# Acknowledgements

Improving Steam System Performance: A Sourcebook for Industry was developed under the BestPractices activity for the U. S. Department of Energy’s (DOE) Industrial Technologies Program (ITP). BestPractices undertook this project as a series of sourcebook publications. Other topics in this series include: compressed air systems, pumping systems, fan systems, process heating, and motor and drive systems. For more information about DOE’s BestPractices, see ITP and BestPractices in the Where to Find Help section of this publication.

ITP, Lawrence Berkeley National Laboratory, and Resource Dynamics Corporation wish to thank the staff at the many organizations that so generously assisted in the collection of data for this Sourcebook. The Alliance to Save Energy, the Council of Industrial Boiler Operators, the National Insulation Association,and the North American Insulation Manufacturers Association provided valuable assistance in developing, compiling, and reviewing this publication.

The BestPractices Steam activity appreciates the participation of the Steam Technical Subcommittee. Special thanks are extended to its co-chairs, Dr. Anthony Wright, Oak Ridge National Laboratory, and Glenn Hahn, Spirax Sarco, an Allied Partner, for providing extensive technical guidance and reviewthroughout the preparation of this publication. The efforts of these program and committee participants are greatly appreciated.

Additionally, the contributions of the following participants are appreciated for their review of and suggestions for this Sourcebook:

Deborah Bloom, Nalco Company Sean Casten, Turbosteam Corporation Bruce Gorelick, Enercheck Systems Robert Griffin, Enbridge Gas Distribution, Canada Dr. Greg Harrell, Energy, Environment and Resources Center, University of Tennessee-Knoxville Thomas Henry, Armstrong Service Carroll Hooper, Steam Solutions, Inc. James Kumana, Kumana and Associates Andrew W. Larkin, Trigen Energy Corporation Lloyd Mason, Condensate Return Specialists Gil McCoy, EERE Information Center Kelly Paffel, Plant Support & Evaluations, Inc. W. Randall Rawson, American Boiler Manufacturers Association Douglas Riley, Millennium Chemical Thomas Scheetz, BASF John Todd, Yarway Corporation

Prepared for: The United States Department of Energy Industrial Technologies Program

Prepared by: Lawrence Berkeley National Laboratory Washington, DC Resource Dynamics Corporation Vienna, VA

Cover photo credit: NREL/PIX 05559. The Leathers geothermal power plant located in the Salton Sea, California. Photo by Warren Gretz.

### Acknowledgements i
Table of Contents ii List of Figures and Tables iii



## Quick Start Guide

Section 1: Steam System Basics
Why Steam? 3 Steam System Operation 3

Generation 5

Distribution 11

End Use 15 Recovery 21



## Section 2: Performance Improvement Opportunities

Overview 25 Systems Approach 25 Common Performance Improvement Opportunities 25 BestPractices Steam System Performance Tools 26 Steam System Training 28 Overview of Financing Steam System Improvements 29



## Section 3: Where to Find Help
The Industrial Technologies Program and BestPractices 33 Directory of Contacts 36

Resources and Tools 37



## Appendices
Appendix A: Glossary of Terms 57 Appendix B: Steam Tip Sheets 61 Appendix C: Guidelines for Comment 101 

# Contents

ii A Sourcebook for Industry 1

3

25

33

55

### iii Improving Steam System Performance 

## List of Figures
Figure 1. Steam System Schematic 4 Figure 2. Firetube Boiler 5 Figure 3. Watertube Boiler 6 Figure 4. Thermostatic Steam Trap with a Bellows Element 13 Figure 5. Thermostatic Steam Trap with a Bimetallic Element 13 Figure 6. Inverted Bucket Steam Trap 14 Figure 7. Float and Thermostatic Steam Trap 14 Figure 8. Thermodynamic Disc Steam Trap 14 Figure 9. Shell and Tube Heat Exchanger 18 Figure 10. Components of a Plate and Frame Heat Exchanger 18 Figure 11. Configuration of a Jacketed Kettle Heat Exchanger 18 Figure 12. Thermocompressor Operation 20 Figure 13. Condensate Receiver Tank and Pump Combination 22 Figure 14. Flash Steam Recovery Vessel 23



## List of Tables
Table 1. Key IOF Steam End-Use Equipment 16 Table 2. Common Performance Improvement Opportunities for the Generation, Distribution, and Recovery Parts of Industrial Steam Systems 26

### 1 This Sourcebook is designed to provide steam system users with a reference that describes the basic steam system components, outlines opportunities for energy and performance improvements, and discusses the benefits ofa systems approach in identifying and implementing these improvement opportunities. The Sourcebook is divided into three main sections as outlined below.

This Sourcebook is not intended to be a comprehensive technical guide on improving steam systems, but rather a document that makes users aware of potential performance improvements, provides some practical guidelines, and directs the user to helpful resources. A systems approach analyzes the supply and the demand sides of the system and how they interact, essentially shifting the focus from individual components to total system performance. The cost-effective operation and maintenance of a steam system require attention not only to the needs of individual pieces of equipment, but also to the system as a whole. Often, operators are so focused on the immediate demands of the equipment, they overlook the broader question of how system parameters affect the equipment.

◆ 

### Section 1: Steam System Basics For users unfamiliar with the basics of steam systems, or for users seeking a refresher, a brief discussion of the terms, relationships, and important system design considerations is provided. Users already familiar with industrial steam system operation may want to skip this section. This section describes steam systems using four basic parts: generation, distribution, end use, and recovery. ◆ 

### Section 2: Performance Improvement Opportunities This section discusses important factors that should be considered when industrial facilities seek to improve steam system performance and to lower operating costs. This section also providesan overview of the financial considerations related to steam system improvements. Additionally, this section discusses several resources and tools developed through the U. S. Department of Energy’s (DOE) BestPractices Steam activities to identify and assess steam system improvement opportunities.

◆ 

### Section 3: Where to Find Help This section provides a directory of associations and other organizations involved in the steam system marketplace. This section also provides a description of the BestPractices Steam activities, a directory of contacts, and a listing of available resources and tools, such as publications, software, training courses, and videos.

◆ 

### Appendices The Sourcebook includes three appendices. Appendix A is a glossary defining terms used in steam systems. Appendix B contains a series of steam system tip sheets. Developed through DOE’s BestPractices Steam activities, these tip sheets discuss common opportunities thatindustrial facilities can use to improve performance and reduce fuel use. Appendix C provides guidelines for submitting suggested changes and improvements to the Sourcebook.

A Sourcebook for Industry 

# Quick Start Guide Quick Start Guide

### 2 Improving Steam System Performance

### 3 

# Why Steam? There are three principal forms of energy used in industrial processes: electricity, direct-fired heat, and steam. Electricity is used in many different ways, including mechanical drive, heating, and electrochemical reactions. Direct-fired energy directly transfers the heat of fuel combustion to a process. Steam provides process heating,pressure control, mechanical drive, and component separation, and, is a source of water for many process reactions.

Steam has many performance advantages that make it an indispensable means of delivering energy. These advantages include low toxicity, ease of transportability, high efficiency, high heat capacity, and low cost with respect to the other alternatives. Steam holds a significant amount of energy on a unit mass basis (between 1,000 and 1,250 British thermal units per pound [Btu/lb]) that can be extracted as mechanical work through a turbine or as heat for process use. Since most of the heat content of steam is stored as latent heat, large quantities of heat can be transferred efficiently at a constant temperature,which is a useful attribute in many process heating applications.

Steam is also used in many direct contact applications. For example, steam is used as a source of hydrogen in steam methane reforming, which is an important process for many chemical and petroleum refining applications. Steam is also used to control the pressures and temperatures of many chemical processes. Other significant applications of steam are to strip contaminants from a process fluid, to facilitate the fractionation of hydrocarbon components, and to dry all types of paper products. 

### The many advantages that are available from steam are reflected in the significant amount of energy that industry uses to generate it. For example, in 1994, industry used about 5,676 trillion Btu of steam energy, which represents about 34% of the total energy used in industrial applications for product output. 1

Steam use in the Industries of the Future 2 is especially significant. For example, in 1994, the pulp and paper industry used approximately 2,197 trillion Btu of energy to generate steam, accounting for about 83% of the total energy used by this industry. The chemicals industry used approximately 1,855 trillion Btu of energy to generate steam, which represents about 57% of the total energy used in this industry. The petroleum refining industry used about 1,373 trillion Btu of energy to generate steam, which accounts for about 42% of this industry’s total energy use. 3

◆ 

### Steam System Operation This Sourcebook uses four categories to discuss steam system components and ways to enhancesteam system performance: generation, distribution, end use, and recovery. These four areas follow the path of steam as it leaves the boiler and returns via the condensate return system.



### Generation Steam is generated in a boiler or a heat recovery steam generator by transferring the heat of combustion gases to water. When water absorbs enough heat, it changes phase from liquid to steam. In some boilers, a superheater further increases the energy content of the steam. Under pressure, the steam then flows from the boiler or steam generator and into the distribution system.

A Sourcebook for Industry 

# Section 1: Steam System Basics

1 Arthur D. Little, Overview of Energy Flow for Industries in Standard Industrial Classifications 20–39, December, 2000. 2 DOE’s Industries of the Future (IOF) include: aluminum, chemicals, forest products, glass, metal casting, mining,

petroleum refining, and steel. 3 Resource Dynamics Corporation estimates. 

### Steam System Basics

### 4 ◆ 

### Distribution The distribution system carries steam from the boiler or generator to the points of end use. Many distribution systems have several take-off lines that operate at different pressures. These distribution lines are separated by various types of isolation valves, pressure-regulating valves, and, sometimes, backpressure turbines. A properly performing distribution system delivers sufficientquantities of high quality steam at the right pressures and temperatures to the end uses. Effective distribution system performance requires propersteam pressure balance, good condensate drainage, adequate insulation, and effective pressure regulation.

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### End Use There are many different end uses of steam. Examples of steam’s diverse uses include processheating, mechanical drive, moderation of chemical reactions, and fractionation of hydrocarbon components. Common steam system end-use equipment includes heat exchangers, turbines, fractionating towers, strippers, and chemical reaction vessels.

In a heat exchanger, the steam transfers its latent heat to a process fluid. The steam is held in the heat exchanger by a steam trap until it condenses, at which point the trap passes the condensate into the condensate return system. In a turbine, the steam transforms its energy to mechanical work to drive rotating machinery such as pumps,compressors, or electric generators. In fractionating towers, steam facilitates the separation ofvarious components of a process fluid. In stripping applications, the steam pulls contaminants out of a process fluid. Steam is also used as a source of water for certain chemical reactions. In steam methane reforming, steam is a source of hydrogen.

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### RecoveryThe condensate return system sends the condensate back to the boiler. The condensate is returned to a collection tank. Sometimes the makeup water and chemicals are added here while othertimes this is done in the deaerator. From the collection tank the condensate is pumped to thedeaerator, which strips oxygen and non-condensable gases. The boiler feed pumps increase the feedwater pressure to above boiler pressure and inject it into the boiler to complete the cycle.

Figure 1 provides a general schematic description of the four principal areas of a steam system. The following sections discuss the components in these areas in greater detail.

Improving Steam System Performance 

### Steam System Basics

Combustion

Gases

Condensate Receiver Tank Pressure Reducing Valve

Feed Pump Steam Trap

Steam Trap Steam Trap Economizer

Combustion Air Condensate Pump Process Heater Process Heater Isolation Valve

Boiler

Deaerator Fuel Combustion Air Preheater

Shell and Tube Heat Exchanger Forced Draft Fan Distribution

Recovery End Use

Figure 1. Steam System Schematic Generation

### 5 

# Generation The generation part of a steam system uses a boiler to add energy to a feedwater supply to generate steam. The energy is released from the combustion of fossil fuels or from process waste heat. The boiler provides a heat transfer surface (generally a set of tubes) between the combustion products and the water. The most important parts of the generating system include the boiler, the fuel supply, combustion air system, feedwater system, and exhaust gases venting system. These systems are related, since problems or changes in one generally affect the performance of the others.

◆ 

### Boilers There are two basic types of boilers: firetube and watertube. The fundamental difference between these boiler types is which side of the boiler tubes contains the combustion gases or the boiler water/steam. Firetube boilers. In firetube boilers, the combustion gases pass inside boiler tubes, and heat istransferred to water on the shell side. A representative firetube boiler is shown in Figure 2. Scotch marine boilers are the most common type of industrial firetube boiler. The Scotch marine boiler is an industry workhorse due to low initial cost, and advantages in efficiency and durability. Scotch marine boilers are typically cylindrical shells with horizontal tubes configured such thatthe exhaust gases pass through these tubes, transferring energy to boiler water on the shell side.

Scotch marine boilers contain relatively large amounts of water, which enables them to respond to load changes with relatively little change in pressure. However, since the boiler typically holds a large water mass, it requires more time to initiate steaming and more time to accommodate changes in steam pressure. Also, Scotch marine boilers generate steam on

A Sourcebook for Industry 

### Steam System Basics

Figure 2. Firetube Boiler4

4 Guideline for Gas and Oil Emission Factors for Industrial, Commercial, and Institutional (ICI) Boilers , American Boiler

Manufacturer’s Association, Arlington, Virginia, 1997.

### 6 the shell side, which has a large surface area, limiting the amount of pressure they can generate. In general, Scotch marine boilers are not used where pressures above 300 psig are required. Today, the biggest firetube boilers are over 1,500 boiler horsepower (about 50,000 lbs/hr). 5

Firetube boilers are often characterized by their number of passes, referring to the number of times the combustion (or flue) gases flow the length of the pressure vessel as they transfer heat to the water. Each pass sends the flue gases through the tubes in the opposite direction. To make another pass, the gases turn 180 degrees and pass back through the shell. The turnaround zones can be either dryback or water-back. Indryback designs, the turnaround area is refractorylined. In water-back designs, this turnaround zone is water-cooled, eliminating the need for the refractory lining. Watertube boilers. In watertube boilers, boiler water passes through the tubes while the exhaust gases remain in the shell side, passing over the tube surfaces. A representative watertube boiler is shown in Figure 3. Since tubes can typically withstand higher internal pressure than the large chamber shell in a firetube, watertube boilers are used where high steam pressures (3,000 pounds per square inch [psi], sometimes higher) are required. Watertube boilers are also capable of high efficiencies and can generate saturated orsuperheated steam. In fact, the ability of watertube boilers to generate superheated steam makesthese boilers particularly attractive in applications that require dry, high-pressure, high-energy steam, including steam turbine power generation.

The performance characteristics of watertube boilers make them highly favorable in process industries, including chemical manufacturing,

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5 1 boiler horsepower = 33,475 Btu/hr 6 Guideline for Gas and Oil Emission Factors for Industrial, Commercial, and Institutional (ICI) Boilers , American Boiler

Manufacturer’s Association, Arlington, Virginia, 1997. Figure 3. Watertube Boiler6

### 7 pulp and paper manufacturing, and refining. Although firetube boilers account for the majorityof boiler sales in terms of units, water-tube boilers account for the majority of boiler capacity. 7

Waste Heat Recovery Boiler (WHRB). These boilers may be either firetube or watertube design and use heat that would otherwise be discarded to generate steam. Typical sources of heat forWHRBs include exhaust gases or high temperature products from an external manufacturing process in refineries and chemical manufacturing facilities, or combustion of a waste fuel in the boiler furnace.

Heat Recovery Steam Generators (HRSGs). HRSGs transfer energy from the exhaust of a gas turbineto an unfired or supplementary fired heat-recovery steam generator to produce steam. Exhaust gases leave the gas turbine at temperatures of 1000°F (538°C) or higher and can represent more than 75% of the total fuel energy input. This energy can be recovered by passing the gases through a heat exchanger (steam generator) to produce hot water or steam for process needs. If the amount of steam needed by the process exceeds the amount produced by simple heat recovery, then supplementary fuel can be burned in the ducting between the gas turbine and the HRSG.

Superheaters



### . Superheaters add energy to steam, resulting in a steam temperature that exceeds the saturation temperature at a specific pressure.Superheaters can be convective or radiant. Radiative superheaters rely on the energy transferred directly from the combustion flame to increase the energy level of the steam, while convective superheaters rely on the transfer of additional energy from the flue gases to the steam.

Economizers. In many boilers, the flue gases still have useful amounts of energy even after they have passed through the boiler. In many of these applications, economizers provide effective methods of increasing boiler efficiency bytransferring the heat of the flue gases to incoming feedwater. There are two principal types of economizers: noncondensing and condensing.Noncondensing economizers are usually air-towater heat exchangers. Since these economizers are not designed to handle flue gas condensation, noncondensing economizers must be operated at temperatures that are reasonably above the dew points of the flue gas components. The dew point of the flue gases depends largely on the amount of water in the gas, which, in turn, is related to the amount of hydrogen in the fuel. For example, to avoid condensation in the exhaust gases produced by burning natural gas, the exhaust gas temperature should typically be kept above 250°F. Condensing economizers are designed to allow condensation of the exhaust gas components. Due to latent heat recovery, these economizers typically extract more energy than do noncondensing economizers. Often, special materials are required.

For more information on economizers, see the Steam Tip Sheet Number 3 titled Use Feedwater Economizers for Waste Heat Recovery in Appendix B.

Combustion air preheaters. Combustion air preheaters are similar to economizers in that they transfer energy from the flue gases back into the system. In these devices, however, the energy is transferred to the incoming combustion air. The efficiency benefit is roughly 1% for every 40°F increase in the combustion air temperature. 8

◆ 

### Boiler Insulation The walls and combustion regions of boilers are typically lined with insulating materials to reduce energy loss and to prevent leakage. There are several types of boiler insulating materials, including brick, refractory, insulation and lagging. The selection and design of boiler insulating materials depends largely on the age and design of the boiler. Since the insulating lining is exposed to high temperatures and is subject to degradation, it should be periodically inspected and repaired when necessary.

◆ 

### Boiler Control System Boiler control systems are designed to protect the boiler and to ensure proper boiler operation. These systems include the combustion control system, flame safeguard, water level control, and fuel control.

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### Steam System Basics

7 GRI, Analysis of the Industrial Boiler Population, Final Report No.-96/0200, 1996. 8 Boiler Efficiency Institute, Boiler Efficiency Improvement , 1991.

### 8 Combustion control system. The combustion control system regulates the fuel air mixture to achieve safe and efficient combustion and maintains steam system pressure. Control systems have varying levels of sophistication. Simple systems use a fixed linkage between the fuel-regulating valve and the combustion air damper. This is called single point positioning. A change in steam pressure makes a proportional change in the combustion air and fuel. Advanced systems rely on signals from transmitters to determine independent fuel valve and air damper positions. This is called a full monitoring system.

For more information, see the Steam Tip Sheet Number 4 titled Improve Your Boiler’s Combustion Efficiency in Appendix B.

Burner flame safeguard system. A flame safeguard system is an arrangement of flame detection systems, interlocks, and relays which will sense the presence of a proper flame in a furnace and cause fuel to be shut off if a hazardous conditiondevelops. Modern combustion systems are closely interlocked with flame safeguard systems andalso pressure-limit switches, low-water level cutoffs, and other safety controls that will stop theenergy input to a boiler when an unsafe condition develops. The flame safeguard system sensesthe presence of a good flame or proper combustion and programs the operation of a burner system so that motors, blowers, ignition, and fuel valves are energized only when they are needed and then in proper sequence.

Safety shutoff valve. Safety shutoff valves isolate the fuel supply to the boiler in response to certain conditions such as low or high gas pressure or satisfied load demand. The type of safety shutoff valves and the settings are often determined by code or insurance requirements.

Water level control. The boiler water level control system ensures a safe water level in the boiler. Typically, the control system provides a signal to the feedwater control valve to regulate the feed rate. Simple water level control systems that only sense water level are single element systems. More complex systems incorporate additional data such as steam flow rate (dual element system) and feedwater flow (triple element system) and will provide better water level control during abrupt load changes. Safety valve. The safety valve is the most important valve on the boiler and keeps the boiler from exceeding its maximum allowable working pressure (MAWP).

Steam pressure control. Steam pressure controls regulate the combustion equipment to maintain a constant pressure in the steam header. As the pressure rises above or falls below the pressure setting, the control adjusts the burner firing rate to bring the pressure back to the setpoint.

Nonreturn valve. The nonreturn valve is a combination shutoff and check valve that allows steam out of the boiler, but prevents backflow from the steam header in the event the boiler pressure drops below that of the header. The valve is opened only when the pressure inside the boiler rises slightly above the steam header pressure.

Steam flow meter. Steam flow meters are helpful in evaluating the performance of the system and can provide useful data in assessing boiler performance, calculating boiler efficiency, and tracking the amount of steam required by the system. In some systems, steam flow meters provide a measurement signal for the boiler control system. Additionally, steam flow meters can be useful in benchmarking efforts.

There are three basic types of steam flowmeters: differential pressure (DP), vortex, and Coriolis. Differential pressure flowmeters rely on the change in pressure as steam flows by an element such as a nozzle, orifice, or venturi. This pressure difference provides an indication of flow velocity, which, in turn, can be used to determine the flow rate. Vortex flowmeters rely on the principal that flow past an element creates vortices that have frequencies that correspond to the flow velocity. Coriolis flowmeters rely on tubes placed in the steam flow path that twist according to the velocity of the flow.

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### Boiler Feedwater System The boiler feedwater system supplies water to the boiler. Sources of feedwater include returning condensate and makeup water. Feedwater is typically stored in a collecting tank to ensure that a steady supply of heated water is available to the boiler.

Improving Steam System Performance 

### Steam System Basics

### 9 Feedwater flow control valve. A modulating feedwater flow control valve moves up or down in response to the water level transmitter(s). On smaller firetube boilers, it is not uncommon for the feedwater valve to operate in a closed or open position, depending on the water level transmitter signal.

Softener. Softeners remove hardness minerals, such as calcium, magnesium, and iron, from a water supply. The presence of hardness in boiler water leads to many problems, including scale buildup and foaming, which reduce boiler efficiency and can cause tube failure. Softeners reduce this problem through an ion exchange process. As the hard water passes through a chamber filled with resin, an exchange occurs that removes hardness minerals from the water. The sodium that replaces the hardness minerals has a higher solubility in water and generally will not form scale.

Pretreatment equipment. Pretreatment equipment improves the quality of the incoming water sothat it may be used in the boiler without excessive scaling or foaming, which can reduce boiler efficiency and cause tube failure. Pretreatment equipment includes, but is not limited to, clarifiers, filters, softeners, dealkalizers, decarbonators, reverse osmosis (RO) units, and demineralizers.

Deaerator, deaerating heater, and atmospheric deaerator. The presence of oxygen in the boiler system can be a significant problem due to its corrosivity at high temperatures. Deaerators and deaerating heaters use heat, typically steam, to reduce theoxygen content in water. Deaerators and deaerating heaters are typically pressurized tanks thatraise the water temperature to the point of saturation. They also break the incoming water into either fine droplets or thin sheets to facilitate the removal of oxygen and other non-condensable gases. Depending on the design, the feedwater oxygen content can be reduced to levels ranging from 7 to 40 parts per billion (ppb).

Atmospheric deaerators are typically found in smaller, lower-pressure boiler systems. They operate at atmospheric pressure, so the maximum operating temperature is 212°F. Most will operate at temperatures lower than this. Atmospheric deaerators cannot achieve the same level of oxygen removal as deaerators and deaerating heaters, typically providing water with oxygen levels of 0.5 to 1 parts per million (ppm).

In applications that require lower oxygen levels than achievable with a deaerator, deaerating heater, or open feedwater heater, a chemical agent, known as an oxygen scavenger, can be used to remove more oxygen. In most systems, an oxygen scavenger is part of the system’s water treatment program.

For more information on these devices, see the Steam Tip Sheet Number 18 titled Deaerators in Industrial Steam Systems , provided in Appendix B.

Feedwater pump. Feedwater pumps transfer water from the deaerator to the boiler. Feedwater pumps are driven by electric motors or by steam turbines. In a modulating feedwater system, the feedwater pumps run constantly as opposed to an on/off operation in relatively small boilers.

Collecting/Storage tank. The return of condensateis often erratic due to changing steam requirements by the end uses. The condensate is usually returned to a condensate receiver or directly to the deaerator if the system does not have a receiver. Pretreated water may also be stored in a tank prior to use. This provides the boiler system with additi onal water capacity in case the pretreatment equipment malfunctions. The condensate and pretreated water, or makeup, are transferred from the storage tanks to the deaerator prior to being sent to the boiler.

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### Boiler Combustion Air System The combustion air system supplies the oxygennecessary for the combustion reaction. To provide enough air for the amount of fuel used in industrial boilers, fans are typically required. Dampers, inlet valves, or variable speed drives typically control the amount of air allowed into the boiler.

Forced draft fan. A forced draft fan is located at the inlet of a boiler and pushes ambient air into the burner region, ensuring that adequate air is delivered to the combustion process. These fans either pull air directly from the boiler room or connect to a duct system that allows outside air to be drawn into the boiler



### .

A Sourcebook for Industry 

### Steam System Basics

### 10 Induced draft fan. Induced draft fans are located on the outlet gas side of the boiler and pull flue gases out. The induced draft fan creates a slightly negative furnace pressure that is controlled by outlet dampers on the boiler. In some systems where a bag house, mechanical collector, or precipitator is involved, special considerations should be given in sizing and selection of this fan.

Damper. Dampers control the amount of air allowed into and out of a combustion chamber. Dampers, in combination with fuel regulating devices, are positioned by the combustion control system to achieve certain fuel-to-air ratios. Dampers on the boiler outlet are used to regulate the negative furnace draft.

◆ 

### Boiler Fuel System There are many different types of fuels used in boilers, requiring several different types of fuel handling systems. Fossil fuels such as coal, oil, and gas are most commonly used. Waste fuels are used in many industries, particularly the forestproducts, petroleum refining, and chemical manufacturing industries where there is an available supply of waste products such as bark, wood chips, black liquor, and refinery gas.

Fuel regulating valve. In gaseous and liquid fuels, regulating valves control the fuel delivered to the boiler. In many systems, these valves can be quickly shut in response to an operating problem.

Fuel. The fuel types that are commonly used in boilers include natural gas, coal, propane, fuel oils, and waste fuels (for example, black liquor, bark, and refinery gas). Fuel type significantly affects boiler operation, including efficiency, emissions, and operating cost. Natural gas accounts for about 36% of the total U.S. industry boiler capacity. Coal accounts for about 14% of the boiler capacity. Fuel oils account for about 21%. Other fuels, which include waste fuels, account for about 29% of the boiler capacity. 9

Fuel flow meter. Fuel meters measure the amount of fuel delivered to a boiler. Fuel meters provide essential data in determining boiler efficiency. Since fuel flow meters measure volume or mass of fuel, it is important to know the energy content of the fuel when determining boiler efficiency. For more information, see the Steam Tip Sheet Number 15 titled Benchmark the Fuel Cost of Steam Generation in Appendix B.

Burner. Burners combine the fuel and air to initiate combustion. There are many different types of burners due to the many different types of fuels. Additionally, burners have different performance characteristics and control requirements. Some burners are on/off while others allow precise setting of the fuel:air mixture over a range of conditions. Some burners can fire different types of fuel, allowing boiler operation to continue despite the loss of one fuel supply.

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### Boiler Blowdown System The boiler blowdown system includes the valves and the controls for the continuous blowdown and bottom blowdown services. Continuous blowdown removes a specific amount of boiler water (often measured in terms of percentage of feedwater flow) in order to maintain a desiredlevel of total dissolved solids in the boiler. Setting the flow for the continuous blowdown is typically done in conjunction with the water treatment program. Some continuous blowdown systems rely on the input of sensors that detect the level of dissolved solids in the boiler water.

The bottom blowdown is performed to remove particulates and sludge from the bottom of the boiler. Bottom blowdowns are periodic and are typically performed a certain number of times per shift or according to a set schedule. In some systems, bottom blowdowns are controlled by an automatic timer. Bottom blowdown should never be permitted unless it is recommended by the boiler manufacturer. This is because in higher pressure boilers, especially those above 700 pounds per square inch gauge (psig), bottom blowdown may cause water starvation in some portions of the boiler circuit.



### Boiler blowdown heat exchangers and flash tank. The continuous blowdown water has the same temperature and pressure as the boiler water. Before this high energy water is discharged into the environment, it is often sent to a heat exchanger and flash tank. Flash tanks permit the recovery of low-pressure flash steam, which can be used in deaeration or process heating. They also permit the use of a smaller heat exchanger

Improving Steam System Performance 

### Steam System Basics

9 Derived from GRI, Analysis of the Industrial Boiler Population, Final Report No.-96/0200, 1996.

### 11 than would be required without the flash tank. Blowdown heat exchangers are most often used to preheat boiler makeup water.

For more information on boiler blowdowns, see the Steam Tip Sheets Numbers 9 and 10 titled Minimize Boiler Blowdown , and Recover Heat from Boiler Blowdown in Appendix B.



# Distribution

The distribution system transports steam from the boiler to the various end uses. Although distribution systems may appear to be passive, in reality, these systems regulate the delivery of steam and respond to changing temperature and pressure requirements. Consequently, proper performance of the distribution system requires careful design practices and effective maintenance. The piping should be properly sized, supported, insulated, and configured with adequate flexibility.Pressure-regulating devices such as pressurereducing valves and backpressure turbines should be configured to provide proper steam balance among the different steam headers. Additionally, the distribution system should be configured to allow adequate condensate drainage, which requires adequate drip leg capacity and proper steam trap selection. Steam distribution systems can be broken down into three different categories: buried pipe, above-ground, and building sections, and selection of distribution components (piping, insulation, etc.) can vary depending on the category.

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### Piping Steam piping transports steam from the boiler to the end-use services. Important characteristics of well-designed steam system piping are that it is adequately sized, configured, and supported. Installation of larger pipe diameters may be more expensive, but can create less pressure drop for a given flow rate. Additionally, larger pipe diameters help to reduce the noise associated with steam flow. As such, consideration should be given to the type of environment in which the steam piping will be located when selecting the pipe diameter. Important configuration issues are flexibility and drainage. With respect to flexibility, piping (especially at equipment connections), needs to accommodate thermal reactions during system start-ups and shutdowns. Additionally, piping should be equipped with a sufficient number of appropriately sized drip legs to promote effective condensate drainage. Additionally, the piping should be pitched properly to promote the drainage of condensate to these drip lines. Typically, these drainage points experience two very different operating conditions, normal operation and start-up; both load conditions should be considered in the initial design.

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### Insulation Thermal insulation provides important safety, energy savings, and performance benefits. In terms of safety, insulation reduces the outer surface temperature of the steam piping, which lessens the risk of burns. A well-insulated system also reduces heat loss to ambient workspaces, which can make the work environment more comfortable. Consequently, the energy saving benefits include reduced energy losses from the steam system and reduced burden on the cooling systems that remove heat from workspaces. In addition to its safety and energy benefits, insulation increases the amount of steam energy available for end uses by decreasing the amount of heat lost from the distribution system.

Important insulation properties include thermalconductivity, strength, abrasion resistance, workability, and resistance to water absorption. Thermal conductivity is the measure of heat transfer per unit thickness. Thermal conductivity of insulation varies with temperature; consequently, it is important to know the right temperature rangewhen selecting insulation. Strength is the measure of the insulation’s ability to maintain itsintegrity under mechanical loads. Abrasion resistance is the ability to withstand shearing forces. Workability is a measure of the ease with which the insulation is installed. Water absorption refers to the tendency of the insulation to hold moisture. Insulation blankets (fiberglass and fabric) are commonly used on steam distribution components (valves, expansion joints, turbines, etc.) to enable easy removal and replacement for maintenance tasks.

Some common insulating materials used in steam systems include calcium silicate, mineral fiber, fiberglass, perlite, and cellular glass. The American Society for Testing and Materials (ASTM) provides standards for the required properties of these and other insulation materials. Additionally, the North American Insulation Manufacturers Association (NAIMA) has developed a software

A Sourcebook for Industry 

### Steam System Basics

### 12 program titled 3E Plus that allows users to determine the energy losses associated with various types and thicknesses of insulation. The 3E Plus program facilitates the assessment of various insulation systems to determine the most cost-effective solution for a given installation. See Section 2, page 27 for more about 3E Plus Insulation software, which can help steam users assess insulation opportunities.

For more information on insulation, refer to Steam Tip Sheets Numbers 2 and 17 titled Insulate Steam Distribution and Condensate Return Lines and InstallRemovable Insulation on Uninsulated Valves and Fittings. Both can be found in Appendix B.

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### Valves In steam systems, the principal functions of valves are to isolate equipment or system branches, toregulate steam flow, and to prevent overpressurization. The principal types of valves used in steam systems include gate, globe, swing check, pressure reducing, and pressure relief valves. G ate, globe, and swing check valves typically isolate steam from a system branch or a component. Pressure reducing valves (PRV) typically maintain certaindownstream steam pressure conditions by controlling the amount of steam that is passed. These reducing valves are often controlled by transmitters that monitor downstream conditions. Pressurerelief valves release steam to prevent overpressurization of a system header or equipment.

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### Steam Separators In some steam systems, wet steam is generated. This wet steam contains water droplets that can reduce the effectiveness of the steam system. Water droplets erode turbine blades and passages,and pressure reducing valves, thus reducing efficiency and life. Furthermore, liquid water can significantly reduce heat transfer rates in heat exchange components, as well as result in water hammer. Removing water droplets before they reach end-use equipment is necessary.

Steam separators remove water droplets, generally relying on controlled centrifugal flow. This action forces the entrained moisture to the outer wall where it is removed from the separator. The means of moisture removal could be a steam trap or a drain. Some manufacturers include the trap as an integral part of the unit. Additional accessories include water gauge connections, thermometer connections, and vent connections.

Steam separators can be installed in either a horizontal or vertical line. They are capable of removing 99% of particulate entrainment 10 microns and larger over a wide range of flows. Separators are often designed in accordance with ASME Code, Section VIII, Division 1 with pressures to 300 psig.

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### Steam Accumulators A steam accumulator is a large insulated pressure vessel, partially filled with hot water (saturated liquid). When steam supply exceeds demand, the excess high-pressure steam is charged into the accumulator through special charging nozzles. The steam is condensed, giving up its latent heat, to raise the pressure, temperature, and heat content of the water body. When the steam demand exceeds the supply, the pressure in the accumulator drops and the additional required steam flashes from the water, taking back the heat previously stored. A simple system of control valves and check valves regulates the charging and discharging. The excess steam is charged quietly and smoothly, and when steam is needed, it is available with the speed of a control valve operation. There is also an accumulator design that stores hot water for use as boiler feedwater.

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### Steam Traps Steam traps are essential for proper distribution system performance. During system start-ups, traps allow air and large quantities of condensate to escape. During system operation, the traps allow collected condensate to pass into the condensate return system, while minimizing the accompanying loss of steam. There are three primary types of traps: thermostatic, mechanical, and thermodynamic. 10

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### Thermostatic Traps Thermostatic traps use temperature differential to distinguish between condensate and live steam. This differential is used to open or close a valve.Under normal operating conditions, the condensate must cool below the steam temperaturebefore the valve will open. Common types of thermostatic traps include bellows and bimetallic traps.

Improving Steam System Performance 

### Steam System Basics

10 The following discussion of steam traps is based extensively on C. B. Oland, Review of Orifice Plate Steam Traps ,

Oak Ridge National Laboratory, January 2001.

### 13 Bellows traps. Bellows traps include a valve element that expands and contracts in responseto temperature changes. Often a volatile chemical such as alcohol or water is inside the element. Evaporation provides the necessary force to change the position of the valve. At start-up, the bellows trap is open due to the relative cold condition. This operating condition allows air to escape and provides maximum condensate removal when the load is the highest. Bellows traps can fail either open or closed. The configuration of a bellows steam trap is shown in Figure 4.

Bimetallic traps. Bimetallic traps rely on the bending of a composite strip of two dissimilar metals to open and close a valve. Air and condensatepass freely through the valve until the temperature of the bimetallic strip approaches the steamtemperature. After steam or relatively hot condensate heats the bimetallic strip and causes it to close the valve, the trap remains shut until the temperature of the condensate cools sufficientlyto allow the bimetallic strip to return to its original shape and thereby open the valve. Bimetallictraps can fail in either the open or closed position. The configuration of a bimetallic steam trap is shown in Figure 5.

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### Mechanical Traps Mechanical traps use the difference in density between condensate and live steam to produce a change in the position of a float or bucket. This movement causes a valve to open or close. There are a number of mechanical trap designs that are based on this principle. They include ball float, float and lever, inverted bucket, open bucket, and float and thermostatic traps.

Ball float traps. Ball float traps rely on the movement of a spherical ball to open and close the outlet opening in the trap body. When no condensate is present, the ball covers the outlet opening, thereby keeping air and steam from escaping. As condensate accumulates inside the trap, the ball floats and uncovers the outlet opening. This movement allows the condensate to flow continuously from the trap. Unless they are equipped with a separate air vent, ball float traps cannot vent air on start-up.

Float and lever traps. Float and lever traps are similar in operation to ball float traps except the ball is connected to a lever. When the ball floats upward due to accumulation of condensate inside the trap body, the attached lever moves and causes a valve to open. This action allows condensate to continuously flow from the trap. If the condensateload decreases and steam reaches the trap, downward ball movement causes the valve to close, thereby keeping steam from escaping. Unless they are equipped with a separate air vent, float andlever traps can not vent air on start-up. See the discussion on float and thermostatic traps.

Inverted bucket traps. Inverted bucket traps are somewhat more complicated than float and lever traps. At start-up, the inverted bucket inside the trap is resting on the bottom of the trap body and the valve to which the bucket is linked is wide open. The trap is initially filled with condensate. As steam enters the trap and is captured inside the bucket, it causes the bucket to move 

### upward. This upward movement closes the valve and keeps steam from escaping. When the condensate collects and cools the steam, the bucket moves downward. This movement causes the valve to open, thereby allowing the condensate to escape. Unlike closed float traps, inverted bucket traps have intermittent discharge. These traps can be

A Sourcebook for Industry 

### Steam System Basics

Steam & Condensate In Liquid Condensate & Flash Out Bellows Element

Valve

Seat Steam and/or Hot Condensate Depending on Trap Steam & Condensate In Liquid Condensate & Flash Out Hot or Subcooled Liquid

Condensate Bimetallic Elements

Valve Seat

Figure 4. Thermostatic Steam Trap with a Bellows Element Figure 5. Thermostatic Steam Trap with a Bimetallic Element

### 14 Steam System Basics

Improving Steam System Performance depleted of their condensate seal when applied in superheated steam service. If this occurs, the trap will continuously discharge live steam. This trap type is not recommended for superheatedsteam service, unless special installation conditions are met. The configuration of an inverted bucket steam trap is shown in Figure 6.

Open bucket traps. Open bucket traps consist of an upright bucket that is attached to a valve. At start-up, the bucket rests on the bottom of the trap body. In this position, the valve is wide open. As condensate accumulates in the trap body on the outside of the bucket, the bucket floats upward, causing the valve to close. When sufficient condensate accumulates outside the bucket, it spills over the top and fills the inside of the bucket. At this time, the bucket sinks, causing the valve to open. This trap is also prone to failure when applied in superheated steam service because of the loss of the condensate seal. Like inverted bucket traps, open bucket traps have intermittent discharge.

Float and Thermostatic (F&T) traps. Float and thermostatic (F&T) traps are similar to float and lever traps except they include a thermostatic element that allows air to be discharged at start-up and during operation. The thermostatic elements used in these traps are the same as those used in thermostatic traps. The configuration of a float and thermostatic steam trap is shown in Figure 7.

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### Thermodynamic TrapsThermodynamic traps use the difference in kinetic energy (velocity) between condensate and live steam to operate a valve. The disc trap is the most common type of thermodynamic trap, but piston or impulse traps are sometimes used. Disc traps. Disc traps use the position of a flat disc to control steam and condensate flow. When condensate flows through the trap, the disc is raised, thereby causing the trap to open. As steam and air pass through the trap, the disc moves downward. The force that causes the disc to move downward is generated by the difference in pressure between the low-velocity steam above the disc and the high-velocity steam that flows through the narrow gap beneath the disc. Disc traps commonly have an intermittent discharge and, when they fail, they normally fail open. The configuration of a disc steam trap is shown in Figure 8. Generally, the air removal capability of this trap type is poor unless equipped with additional components (like the float and thermostatic trap).

Piston traps. Piston or impulse traps utilize the heat energy in hot condensate, and the kinetic energy in steam, to open and close a valve. Like disc traps, piston traps are phase detectors that sense the difference between a liquid and gas or vapor. They continuously discharge any air and condensate. Their primary failure mode is open. Vent Hole Seat Steam Spaces Condensate Level Steam Bubbles

Inverted Bucket Valve

Lever Liquid Condensate & Flash Out Seat Air Vent

Valve

Float Lever Steam Space

Condensate Level

Liquid Condensate & Flash Out

Steam & Condensate In Liquid Condensate & Flash Out Valve Disc Outlet Port

Seating Surface Inlet Port
Bonnet Chamber Flash Vapor Closes Valve Disc Steam & Condensate In Steam & Condensate In

Figure 6. Inverted Bucket Steam Trap Figure 7. Float and Thermostatic Steam Trap

Figure 8. Thermodynamic Disc Steam Trap

### 15 Lever traps

. Lever traps are a variation of the thermodynamic piston trap. They operate on the same principal as a piston trap but with a lever action to pass large amounts of condensate and air on a continuous basis. Their primary failure mode is open.

Orifice traps. Orifice traps are of two basic types:orifice plate and short tube. Both trap types operate under the exact same principles. A simple orifice plate steam trap consists of a thin metal plate with a small-diameter hole (orifice) drilled through the plate. When installed, condensate that accumulates is continuously removed as the steam pressure forces the condensate through the orifice. During conditions when no condensate is present, a limited amount of steam flows through the orifice. The report Review of Orifice Plate Steam Traps on page 49 of the Where to Find Help section provides information for making informed decisions about when orifice plate steam traps should be considered for use in new or existing steam systems.

Additional information regarding steam traps is available in the Steam Tip Sheet Number 1 titled Inspect and Repair Steam Traps, found in Appendix B.

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### Steam Meters The use of flowmeters within the distributionsystem can provide important data for monitoring the efficiency of a process or an end use. Tracking the amount of steam required can be particularly useful in benchmarking efforts. The types of steam flowmeters are discussed in the Generation Section.



# End Use

Steam system end-use equipment transfers steam energy into other forms of useful energy. Common end-use equipment includes heat exchange devices to transfer thermal energy and turbines to recover mechanical energy. In manufacturing industries, steam end uses often directly support production, making their performance and reliability essential to plant productivity. Improvements in end-use efficiency and effectiveness also tend to result in better performance and increased reliability. There is a wide range of end-use equipment, largely due to the advantages of steam that are discussed in the Introduction. Some of the major end-use components are discussed in this section.

For the purposes of this discussion, steam end-use equipment is grouped into three basic categories:

■ Industries of the Future 11 (IOF) key end-use equipment

■ Conditioning and control equipment

■ Additional equipment.

The key IOF equipment category includes the largest uses of steam in those industries. Although IOF facilities use steam for other services as well, the key end uses account for the largest amount of steam use. The conditioning equipment category includes equipment that facilitates the effective use of steam. The additional equipment category includes equipment that is used in other industries and, though significant, does not account for most of the steam use in IOF industries.



### Industries of the Future Key End-Use Equipment In the three IOF industries of forest products, petroleum refining, and chemicals, steam accounts for the largest amount of end-use energy. In another IOF industry, steel production, steam represents a significant amount of end-use energy and is used to generate most of that industry’s on-site electric power. Table 1 provides a list of key steam-supplied end-use equipment for IOF industries.

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### Condensers In steam applications, condensers are associatedwith condensing steam turbines and with multiple stage ejector systems. In steam turbine applications, condensers typically operate under a vacuum. They remove energy from the exhaust steam, allowing it to be recovered as condensate. In steam ejector applications, condensers increase the effectiveness of the ejectors by condensing both the motive steam and condensables pulled from the process, reducing the amount of motive steam required.

Condensers can be surface type or barometric. Surface condensers are supplied with cooling water that circulates through condenser tubes, providing a cool surface area that causes steam condensation. The condensate is typically

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### Steam System Basics

11 Industries of the Future (IOF) include: aluminum, chemicals, forest products, glass, metal casting, mining, petroleum refining, and steel.

### 16 collected in a condensate well, and pumped intothe condensate return system. Barometric condensers rely on direct contact between the cooling water and the steam. In petroleum refiningand chemical manufacturing applications, condensers are also used to condense components from gaseous mixtures. In these applications, the condensers use a cooling medium to extract energy from the gases and collect the condensed components.

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### Distillation TowersThe petroleum refining and chemical manufacturing industries use large amounts of steam to facilitate the separation of crude oil or chemical feedstocks into various components. This separation process relies on differences in the boilingpoints of these hydrocarbon components. Fractionating towers use a furnace to heat crude oil above 700°F. As the volatile components boil off and rise up the tower, they cool and condense on trays. Steam is injected into the bottom of these towers to reduce the partial pressures of the hydrocarbons, which facilitates their separation, and to reduce coke formation on tray and tower surfaces.

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### DryersDryers reduce the water content of a solid. Dryers account for the largest end use of steam in the pulp and paper industry. 12 The chemical

Improving Steam System Performance 

### Steam System Basics

Equipment Process Application Industry Condenser Steam turbine operation Aluminum, Chemical Manufacturing, Forest Products, Glass, Metal Casting, Petroleum Refining, and Steel Distillation tower Distillation, fractionation Chemical Manufacturing, Petroleum Refining Dryer Drying Forest Products Evaporator Evaporation/concentration Chemical Manufacturing, Forest Products Petroleum Refining Process heat Alkylation, Process air heating, Process water Aluminum, Chemical Manufacturing, Forest exchanger heating, Gas recovery/Light ends distillation, Products, Glass, Metal Casting, Petroleum Isomerization, Storage tank heating Refining, and Steel Visbreaking/Coking Reboiler Fractionation Petroleum Refining Reformer Hydrogen generation Chemical Manufacturing, Petroleum Refining Separator Component separation Chemical Manufacturing, Forest Products, Petroleum Refining Steam ejector Condenser operation, Vacuum distillation Aluminum, Chemical Manufacturing, Forest Products, Glass, Metal Casting, Petroleum Refining, and Steel Steam injector Agitation/blending, Heating Chemical Manufacturing, Forest Products, Petroleum Refining Steam turbine Power generation, Compressor mechanical Aluminum, Chemical Manufacturing, Forest drive, Hydrocracking, Naphtha reforming, Products, Glass, Metal Casting, Petroleum Pump mechanical drive, Feed pump Refining, and Steel mechanical drive Stripper Distillation (crude and vacuum units), Chemical Manufacturing, Petroleum Refining Catalytic cracking, Asphalt processing, Catalytic reforming, Component removal, Component separation, Fractionation, Hydrogen treatment, Lube oil processing Thermocompressor Drying, Steam pressure amplification Forest Products 

### Table 1. Key IOF Steam End-Use Equipment

12 Giese & Associates, Scoping Study of the Pulp and Paper Industry, EPRI, 1988.

### 17 manufacturing, textiles, and food processing industries also use large amounts of steam for drying. Dryers can be indirect or direct. Indirect dryers remove moisture thermally as energy is transferred from condensing steam, flue gases, or high temperature process fluid to the product being dried. Common indirect dryer types are coil and rotating drum. Direct dryers use hot gases that have been heated with steam or flue gases to directly contact and dry a product.

Dryers, like evaporators, can be arranged in multiple-stage configurations. Multiple-stage steamdryers use a cascading set of steam pressures, allowing steam released from an upstream stage to supply steam to the next stage. In many multiple-stage dryers, thermocompressors are used to increase the steam pressure of downstream-effect stages.

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### Evaporators Evaporators reduce the water content of a liquid, generally by heating it with steam in order to concentrate the product. Evaporators are used extensively in industries such as food processing, chemical manufacturing, steel, forest products, and textiles.

In most cases, evaporators are shell and tube heat exchangers with the steam on the shell side and the product being concentrated in the tubes. Evaporators can be single effect or multiple effect. A single-effect evaporator uses steam at one set of pressure and temperature conditions to boil off the vapor from a product. Multiple-effect evaporators take the vapor produced from one evaporator and use it to heat the product in a lower-pressureevaporator. Multiple-effect evaporators are generally more efficient at concentrating a fluid than single-effect evaporators.

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### Heat Exchangers Heat exchangers transfer thermal energy from one fluid to another. In manufacturing facilities, steam is a common source of heat for many reasons, some of which are discussed in the Introduction. There is a wide range of heat exchanger designs that use steam, largely due to the wide range of products that are heated with steam. Many process and product considerations must be incorporated into the selection of a heat exchanger. Some basic heat exchanger types are discussed below, including:

■ Tubular

■ Plate and frame

■ Jacketed

■ Coil.

Tubular heat exchanger. Tubular heat exchangers are tube bundles that are surrounded by the heated or heating medium. This type of heat exchanger includes finned tube and shell and tube designs as shown in Figure 9. Finned tube heat exchangers are often used to heat air for drying and space heating applications. Shell and tube heat exchangers are often used for liquid heating and evaporation. Since the tube side of shell and tube heat exchangers can be designedto withstand high pressures, sometimes exceeding 1,500 psig, heat exchangers of this type are often used in high temperature and high-pressure applications.

Plate and frame heat exchanger. In plate and frame heat exchangers, the two heat exchange fluids are separated by plates. The plates are corrugated, or ridged, as shown in Figure 10, to increase the surface area available for heat transfer. Plate andframe heat exchangers are often used in lowviscosity applications, where the risk of clogging is less severe. The plate ends are typically sealed by gasketed covers that can be removed to allow disassembly and cleaning. This heat exchanger type is used when temperatures and pressures are moderately low, typically below 300°F and 370 psi. Plate and frame heat exchangers also have a common design variation that has the plates welded or brazed together. This allows higher temperature service but eliminates the possibility of mechanical cleaning.

Jacketed heat exchangers. Jacketed heat exchangers use an enclosure to surround the vessel that contains the heated product. A common example of a jacketed heat exchanger is the jacketed kettle. A representation of a jacketed heat exchanger is shown in Figure 11. Jacketed heat exchangers are practical for batch processes and for product types that tend to foul or clog tube bundles or coils.

A Sourcebook for Industry 

### Steam System BasicsCoil heat exchangers. Coil heat exchangers characteristically use a set of coils immersed in themedium that is being heated. Coil heat exchangers are generally compact, offering a large heat transfer area for the size of the heat exchanger.

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### Reboilers Reboilers are typically used in distilling processes to increase component separation. Reboilers use heat, often provided by steam, to evaporate the volatile components of a product that has been drawn from a fractionating tower. These volatile components are sent downstream for further processing. The residual components are sent back into the fractionating tower or sent on to a vacuum distillation process. There are several types of reboilers, including jacketed kettle, kettle, internal reboiler, and thermosyphon reboiler. These designs differ from one another in the way the product is heated with steam. ◆ 

### Reformers Steam reformers are used to generate hydrogen, typically from a hydrocarbon feedstock such as methane (the largest component of natural gas). In turn, hydrogen is used in manypetroleum refining and chemical manufacturing processes. Reformers use steam for both energy and as a source of hydrogen. Steam is injectedwith the hydrocarbon feedstock to initiate the following reaction:

Reformers often have secondary stages that are used to convert the carbon monoxide to carbon dioxide and additional hydrogen. Although large amounts of steam are used throughout the reforming processes, steam is also generated by the reformers and is sometimes exported for other uses.

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### Steam Ejectors Steam ejectors use steam flow through a nozzleto create a vacuum (similar in operation to thermocompressors). They are used in several differenttypes of system applications and process equipment. Low-pressure conditions promote the evaporation of liquids at reduced temperatures.



### 18 Steam System Basics

Improving Steam System Performance Tube Side Fluid Tube Bundle Tubesheet

Shell Side Fluid Baffles

Plates

Compression Fasteners Frame

Kettle Steam

Condensate Steam Jacket Figure 9. Shell and Tube Heat Exchanger

Figure 10. Components of a Plate and Frame Heat Exchanger Figure 10. Configuration of a Jacketed Kettle Heat Exchanger CH 4 + H 2 O → CO + 3H 2 Methane Steam Carbon Hydrogen monoxide

### 19 Consequently, many chemical manufacturing processes use steam ejectors to increase the concentration of a product. In petroleum refining, steam ejectors are commonly usedin the vacuum distillation of heavy hydrocarbon products. Steam ejectors are also used to initiate and maintain vacuum condition in the condensers of condensing turbines.

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### Steam Injectors Steam injectors are used to inject steam directly into a tank or a pipe containing a process fluid, generally for heating purposes. Many injector types use a nozzle and a diffuser to pull process fluid into the steam before the mixture is injectedinto the process fluid, to promote an even distribution of heat. Important performance characteristics of injectors include accurate control of the amount of steam injected and effective mixing of the steam and process.

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### Steam Turbines Steam turbines are used to drive electric generators or other rotating machinery such as compressors, pumps, and fans. Steam turbines are used in many different system designs, depending on the relative requirements for steam, electricity, or other mechanical loads. Steam turbines provide an effective means of stepping down steam pressure while extracting mechanical work.

Additional information regarding steam turbines is available in Steam Tip Sheets Numbers 15 and 21 titled Benchmark the Fuel Costs of Steam Generation and Consider Steam Turbine Drives for Rotating Equipment , found in Appendix B.

Some turbines have interstage take-offs that allow steam to be extracted at various pressures before reaching the turbine exhaust. Theseextractions provide flexibility in meeting competing requirements of both the steam system and the mechanical load. For example, if the turbine is connected to an electric generator, adjusting the amount of extracted steam can allow more or less electric power to be generated, while making respectively less or more steam available to the plant.

Backpressure turbines. Backpressure turbines exhaust steam at pressures that are higher than atmospheric, and the exhaust steam is then used for other services. By extracting mechanical work from steam, backpressure turbines can provide an efficient means of supplying lower-pressure steam from a high-pressure header.

Condensing turbines. Condensing turbines exhaust steam to vacuum (sub-atmospheric) conditions. This steam is condensed in a heat exchanger, referred to as a condenser, and transferred to the condensate return system. Condensing turbines typically require a source of cooling water to condense the steam.

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### Strippers Steam strippers are used to remove contaminants from a solution. Strippers are commonly foundin petroleum refining and chemical manufacturing applications, where process solutions contain components that have different boiling points and removal of one or more of the components is necessary. Injecting steam into the process solution lowers the partial pressure of volatile components, allowing some of them to vaporize and get transported away with the steam. Steam can also raise the temperature of the mixture,lowering the solubility of the objectionable material and causing it to strip off with the steam.Often, the steam and the contaminants are condensed and separated, allowing recovery of the condensate and disposal or further processing of the contaminant.

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### Thermocompressors Thermocompressors combine high-pressure andlow-pressure steam to form an intermediatepressure steam supply (see Figure 12). Often the low-pressure steam does not have enough energy to be feasibly used; however, discharging it to the condensate return system can be an unnecessaryenergy loss. Thermocompressors use a high-pressure steam source to recover the energy from this low-pressure source, providing an intermediate steam supply that can be feasibly used.

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### Conditioning and Control Equipment Conditioning equipment is generally used to improve the performance of, or to protect the end-use equipment. For example, desuperheaters are often used to control the energy of a steam supply to end-use equipment to reduce the risk of damage to the equipment or to effectively improve temperature control of the process.

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### Steam System Basics

### 20 Desuperheaters



### . The purpose of a desuperheater is to remove the superheat from steam. The majority of heating and process equipment performs more efficiently using saturated rather than super-heated steam. Desuper-heaters inject a very fine mist of high-purity water, such as condensate, into the steam flow. The superheated vapor gives up heat to the water mist, and by doing so, reduces its temperature.

Vacuum breakers. Vacuum conditions can developin a steam system when steam flow into a component or a branch is throttled or shut off. If the rate of downstream steam use exceeds the steamsupply, the pressure decreases and vacuum conditions can form. Vacuum conditions also resultwhen the load on the heat exchanger is significantly less than the heat exchanger capacity. If the pressure in the heat exchanger drops too far, the condensate will not drain from the trap due to a higher pressure on the trap’s downstream side. If uncorrected, the condensate level will rise in the heat exchanger, reducing the available heat transfer area and increasing the risk of corrosion by condensate. Vacuum breakers are pressure-controlled devices that essentially vent a heat exchanger or system branch in which a vacuum has formed. By allowing in air when they open, vacuum breakers restore pressure and allow the condensate to drain.

Air vents. Before start-up, the steam system contains air that must be rem oved. The presence of air in a steam system reduces heat transfer effectiveness and promotes condensate corrosion. Air vents remove this air. Air vents are often thermostatic devices, similar to thermostaticsteam traps that rely on the temperature difference between air and steam. When exposed to the lower temperature air in the system side, the vent opens. As the higher temperature steam reaches the vent, it closes, preventing the escape of steam.

Traps. Steam traps are important to the performance of end-use equipment. Traps provide for condensate removal with little or no steam loss. If the traps do not function properly, excess steam will flow through theend-use device or the condensate will back up into it. Excess steam loss will lead to costly operation whilecondensate backup will promote poor performance and may lead to water hammer. Traps can also remove non-conden sable gases that reduce heat exchanger effectiveness. There are severaldifferent types of steam traps, which are discussed in the Distribution section of this Sourcebook.

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### Insulation End-use equipment, such as heat exchangers and turbines, should generally be insulated due to the significant heat loss that the surface areas of this equipment can provide. The various types of insulation are discussed in the Distributionsection of this Sourcebook. Where end-use equipment requires frequent inspection or maintenance, removable insulation should be considered.

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### Additional Equipment The additional equipment category refers to end uses throughout industry, which, though still significant users of steam, generally account for less steam energy than the key IOF end uses.

Absorption chillers. Absorption chillers provide cooling using an interesting variation of thevapor compression cycle. Instead of a compressor, which is generally used in chillers, absorption chillers exploit the ability of one substance to absorb a refrigerant at one temperature and then release it at another. In ammonia-based systems, water is the absorbent and ammonia is the refrigerant. In lithium bromide-based systems, lithium bromide is the absorbent, while water is the refrigerant. An absorption chiller uses a pump instead of a compressor to increase

Improving Steam System Performance 

### Steam System Basics

Discharge (intermediate

pressure) Motive Steam (high pressure)

Suction (low pressure)

Figure 12. Thermocompressor Operation

### 21 refrigerant pressure. Once it is at the higher pressure, the absorbent/ refrigerant solution isheated, often with steam, which releases the refrigerant. Although absorption chillers generally have lower coefficients of performance (COP) (indicating lower thermodynamic efficiency) than traditionalchillers, they use less electric power per ton of cooling and are well suited for use with steam systems.

Humidifiers. Humidifiers inject steam into an air or other gas source to increase its water vapor content. In humidification, steam is used as a source of both water and energy. Humidificationapplications are found in the chemical manufacturing industry where control of ambient temperature and moisture content are critical for product quality.

Preheat/Reheat air handling coils. Steam is often used in space heating applications to preheat and reheat air. In many HVAC systems, the conditioned air must have both its temperature and humidity adjusted. In preheat applications, steam is used to heat an air supply, which is typically a mixture of return air and outside air. The air is then conditioned to achieve a certainhumidity and temperature. In reheat applications, the air is cooled to a particular dew point to remove water and achieve a desired humidity. As a result, before the air is delivered back to the workspaces, steam coils must reheat the process air stream up to the proper temperature. In both reheat and preheat applications, finned tube heat exchangers are generally used.

Tracing. In tracing applications, steam is used to maintain the temperature of a fluid in a pipe. A common application of tracing lines is to prevent the freezing of a process fluid in piping that runs outside of a temperature controlled area. Since tracing lines are exposed to freezing conditions, proper insulation, steam flow, and condensate drainage are essential to prevent freezing of the tracing lines as well as the process piping.

Meters



### . Steam meters are used to measure steam flow, and are important for tracking the steam use of a particular part of a steam system or a particular end use. Discussion of different meter types is provided in the Steam Generation section of this Sourcebook. 

# Recovery

The recovery components of a steam systemcollect and return condensate back to the generation part of the system. Condensate recovery provides thermal and water treatment benefits.Condensate that is not returned must be compensated for by the addition of makeup water, which is generally much cooler than condensate. Condensate temperature often exceeds 200°F while makeup water temperature is typically between 50°F and 80°F. As a result, the enthalpy difference between condensate and makeup water is generally over 120 Btu/lb, an amount of energy that is often more than 10% of the energy in the boiler generated steam.

Additionally, makeup water is generally treatedwith chemicals that remove minerals and establish certain pH levels in the boiler water and in the system. Reducing the amount of makeup water added to the system reduces chemical use. Additionally, some of the treatment chemicals that are contained in condensate are problematic to a plant’s wastewater treatment facility. I ndustrial steam plants often extend across large areas. Recovering condensate from steam systemsrequires piping, collecting tanks, pumping equipment, and, in many cases, flash steam separators,meters, and filtration/cleanup equipment. However, the cost savings available from avoiding the purchase, treatment, and heating of makeup water often make investments in condensate recovery systems highly feasible.

For more information on condensate recovery, see the Steam Tip Sheet Number 8 titled Return Condensate to the Boiler , provided in Appendix B.

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### Condensate Return Piping Condensate return piping transports condensateas it drains from distribution and end-use equipment piping back to the boiler. Condensate piping should be adequately sized and insulated. Although the installation of larger pipe diameters is more expensive, larger pipes create less pressure drop for a given flow rate; this reduces the load on the condensate pumps. Larger pipe diameters also reduce the noise associated with condensate flow and are more suitable for carrying flash steam. Insulating the condensate piping helps to retain the thermal energy that provides much of the benefits of a condensate recovery system.

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### Steam System Basics

### 22 ◆ 

### Insulation Insulation provides energy savings and safety benefits. In terms of energy savings, insulation reduces heat loss from the condensate piping and recovery equipment surfaces, which can makethe surrounding work environment more comfortable. Reducing this heat loss can also reduce the burden on the cooling systems that support surrounding workspaces. In terms of safety, insulation reduces the outer surface temperature of the piping, which lessens the risk of burns.Important insulation properties and characteristics of piping insulation are discussed in the Distribution section of this Sourcebook.

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### Condensate Receiver Tanks Condensate receiver tanks collect and store condensate. These tanks are usually located remotely around the condensate system and are configured in conjunction with condensate pumps, as shown in Figure 13. Condensate flows can be highly variable due to changes in steam demand, especially during system start-ups. Receiver tanks minimize the effects of this flow variability on condensate pumps by providing storage, which maintains a minimum water level that prevents downstream condensate pumps from running dry. Since many condensate pumps are centrifugal types, it is important to keep a certain suction pressure to prevent cavitation damage. By maintaining a minimum condensate level, receiver tanks provide enough static pressure to avoid cavitation.

Most systems also contain a large condensate receiver tank that collects all the condensate returned from the system. This tank may also be used to store pretreated water.

◆ 

### Condensate PumpsCondensate pumps move condensate from receiver tanks back to the boiler room. Condensate pumps can be driven by electric motors, steam, or compressed air, depending on the availability of these sources. Motor-driven condensate pumps are usually centrifugal type pumps. In many cases,receiver tanks and motor driven pumps are packaged together and equipped with a control system that de-energizes the pump under low water level conditions. Steam or compressed air powered condensate pumps are used where electrical pumps would not be suitable, and are generally pressure powered pumps. Condensate pumps also can be important to the performance of end-use equipment. Effective use of condensate pumps can eliminate condensate back up into end-use equipment, improving process control and reducing potential equipment problems from condensate acidification and water hammer.

◆ 

### Flash Steam Vessels Flash steam vessels allow the recovery of steam from condensate lines, as illustrated in Figure 14. By removing steam from the condensate system, flash steam vessels provide an efficient source of steam to low-pressure end uses. For example, 250°F condensate has a saturation pressure of about 15 psig. Consequently, steam that is separated by flash steam vessels can be used in low-pressure steam applications such as space heating and preheating.

For more information on flash steam vessels, see the Steam Tip Sheet Number 12 titled Flash HighPressure Condensate to Regenerate Low-Pressure Steam provided in Appendix B.

◆ 

### Condensate Meters Condensate meters measure the flow rate of condensate in the return system. Knowing thecondensate flow rate can be helpful in monitoring the condensate system and the condition of steam traps. Condensate meters are often inline rotary types, relying on turbine or scroll rotation to measure flow rate.

◆ 

### Filtration/Cleanup EquipmentIn many systems, the flow of steam and condensate picks up rust, scale, and trace contaminants

Improving Steam System Performance 

### Steam System Basics

Condensate Pump

Condensate

Receiver Tank

Outlet Inlet

Figure 13. Condensate Receiver Tank and Pump Combination

### 23 that are either carried over from the boiler or that form in carbon steel piping and on copper alloy heat exchange surfaces. Although strainers and filters are used to catch the particulate matter, some contaminants are dissolved in the condensate and can cause problems if returned to the boiler. In systems that require a high level of cleanliness, condensate polishers are used. Condensate polishers use ion exchange to remove these contaminants, preventing the redeposition of these contaminants on boiler surfaces.

A Sourcebook for Industry 

### Steam System Basics

Saturated Vapor Supply

Steam Trap High-Pressure Condensate

Condensate Discharge Level Controller Low-Pressure Flash Vessel

Saturated

Vapor

Saturated

Liquid

Figure 14. Flash Steam Recovery Vessel

### 24 Improving Steam System Performance 

### Steam System Basics

# Section 2: Performance Improvement Opportunities

25 

# Overview

This section of the Sourcebook discusses important factors that should be considered when industrialfacilities seek to improve steam system performance and to lower operating costs. Improving steam system performance requires assessing the entire system, identifying opportunities, and selecting and implementing the most feasible projects. In turn, this requires a systems approach. Similarly, proper selection of the best projects requires quantifying the benefits and costs of each project. Successful implementation of these projects requires the participation of all system stakeholders including production, maintenance,and management. Generally, obtaining management participation requires communication of the analyses in economic terms. To address these considerations, this section of the Sourcebook discusses:

■ The systems approach

■ Common performance improvement opportunities

■ Resources that can help identify and assess opportunities

■ The economics related to steam system improvements.


# Systems Approach

Because of the many industrial uses for steam,there are wide ranges of steam system sizes, configurations, end-use applications, and operating practices. As a result, there are many different ways to improve steam system performance and identify improvement opportunities. In general, performance is most effectively optimized when a systems approach is used.

A systems approach analyzes both the supply anddemand sides of the system and how they interact, essentially shifting the focus from individual components to total system performance. Often, operators are so focused on the immediate demands of the equipment that they overlook the broader issue of how system parameters affect the equipment. Similarly, a common engineering approach is to break a system down into its basic components or modules, optimize the selection orthe design of these components, and then assemble these components to form the system. An advantage to this approach is that it simplifies problems. However, a disadvantage is that it often overlooks the interaction of these components. In contrast, a systems approach evaluates the entire system to determine how the end-use requirements can be most effectively and efficiently served.

A systems approach also recognizes that system efficiency, reliability, and performance are closely related. For example, an efficiency loss such as heat loss across uninsulated pipe surfaces reduces energy available to the end uses and requires boilers to work harder to meet a given demand. Often, energy losses create additional system stresses that accelerate wear and that can create loads for which the system was not originally designed.



# Common Performance Improvement Opportunities

Several steam system improvement opportunities are common to many industrial facilities. These opportunities can be categorized according to thepart of the system in which they are implemented. Common performance opportunities for the generation, distribution, and recovery areas of a steam system are listed in Table 2.

◆ 

### End-Use Improvement Opportunities There are many ways to optimize steam use depending on the process and the equipment. Specific End Uses for Industries of the Future (IOF) steam systems can be found in Table 1 of the End Use section. In some cases, equipment can be installed to make the process more efficient; for example, multiple-stage dryers are often more efficient than single-stage dryers. However, in general, optimizing the efficiency of steam-supplied end uses requires a case-by-case
assessment.

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### Performance Improvement Opportunities

### 26 

# BestPractices Steam System Performance Tools

The U. S. Department of Energy (DOE) BestPractices Steam effort has developed a suite of resources and tools that can be used to identifyand assess steam system improvement opportunities. These resources and tools are described in this section of the Sourcebook. Additional steam improvement resources and tools are identified in the Resources section of the Sourcebook. ◆ 

### Steam System Scoping Tool The Steam System Scoping Tool is a spreadsheet program that can assist steam operation and management personnel to assess their steam systems. The program is intended for use by steam system energy managers and operations personnel in industrial plants. This tool also helps assess steam system operations against identified best practices.

The Steam System Scoping Tool contains seven worksheets:

Improving Steam System Performance Opportunity Description

Generation
Minimize excess air Reduces the amount of heat lost up the stack, allowing more of the fuel energy to be transferred to the steam Clean boiler heat transfer surfaces Promotes effective heat transfer from the combustion gases to the steam Install heat recovery equipment Recovers available heat from exhaust gases and transfers it back into the (feedwater economizers and/or system by preheating feedwater or combustion air combustion air preheaters) Improve water treatment to minimize Reduces the amount of total dissolved solids in the boiler water, which allows boiler blowdown less blowdown and therefore less energy loss Recover energy from boiler Transfers the available energy in a blowdown stream back into the system, blowdown thereby reducing energy loss Add/restore boiler refractory Reduces heat loss from the boiler and restores boiler efficiency Optimize deaerator vent rate Minimizes avoidable loss of steam
Distribution
Repair steam leaks Minimizes avoidable loss of steam Minimize vented steam Minimizes avoidable loss of steam Ensure that steam system piping, Reduces energy loss from piping and equipment surfaces valves, fittings, and vessels are well insulated Implement an effective steam-trap Reduces passage of live steam into condensate system and promotes efficient maintenance program operation of end-use heat transfer equipment Isolate steam from unused lines Minimizes avoidable loss of steam and reduces energy loss from piping and equipment surfaces Utilize backpressure turbines instead Provides a more efficient method of reducing steam pressure for low-pressure of PRVs services
Recovery Optimize condensate recovery Recovers the thermal energy in the condensate and reduces the amount of makeup water added to the system, saving energy and chemicals teatment Use high-pressure condensate to Exploits the available energy in the returning condensate make low-pressure steam 

### Table 2. Common Performance Improvement Opportunities for the Generation, Distribution, and Recovery Parts of Industrial Steam Systems Performance Improvement Opportunities

### Performance Improvement Opportunities

A Sourcebook for Industry 1. Introduction—provides instructions on how to use the guide and what is indicated by the results. 2. Basic data—prompts the user to answer general questions such as the amount of fuel used, amount of steam generated, and other general system data. 3. System profiling—assesses how the user tracks steam costs, benchmarks steam use, and measures important general operating parameters. 4. Operating practices of the total system— queries the user regarding practices such as trap maintenance, water treatment, insulation condition, leak repair, and general equipment inspection. 5. Operating practices of the boiler plant— queries the user on boiler efficiency, heat recovery equipment, steam quality, and general boiler operation.6. Operating practices of the distribution, enduse, and recovery portions of the steam system—queries the user about the use of pressure reducing valves, condensate recovery,and the use of condensate to generate lowpressure steam. 7. Summary sheet—provides scores based on user responses.

◆ 

### Steam System Survey Guide The Steam System Survey Guide is a reference document that is intended for use by plant energy managers and system operations personnel. The Survey Guide provides a technical basis for identifying and assessing many potential steam system improvement opportunities. Although several of these opportunities can be identified directly with the survey guide, others require more sophisticated measurements and data gathering methods.

The Scoping Tool and the Survey Guide are complementary. The Scoping Tool allows a user to determine how well the system is performing and is also useful in tracking the effectiveness of system improvements. The Survey Guide provides a more quantitative description of the system operation and how to quantify some of the potential steam system improvement opportunities. These tools are available from DOE’s Industrial Technologies Program (ITP) BestPractices Web site at www.eere.energy.gov/industry/bestpractices. The Web site also offers links to other resourcesthat can assist end users in improving the performance and efficiency of their energy-intensive utility systems.

◆ 

### Steam System Assessment Tool The Steam System Assessment Tool allows users to assess potential savings from individualized steam system improvements. Users may input data about the condition of their plant and the Steam System Assessment Tool generates models of various improvement scenarios. Results detail the energy, cost, and emissions savings that a variety of improvements could achieve.

The tool contains all the key features of typical steam systems—boilers, backpressure turbines, condensing turbines, deaerators, letdowns, flash vessels, and feedwater heat exchangers. Themodel analyzes boiler efficiency, boiler blowdown, cogeneration, steam cost, condensate recovery, heat recovery, vent steam, insulationefficiency, alternative fuels, backpressure turbines, steam traps, steam quality, and steam leaks.

◆ 

### 3E Plus Insulation Appraisal Software Because insulation is used in every steam system, its restoration, replacement, or installation are common improvement opportunities. A lack of awareness regarding the energy losses and theassociated costs often results in a low prioritization of restoring or properly installing insulation on steam system surfaces. As a result, a software program known as 3E Plus was developed by the North American Insulation Manufacturers Association (NAIMA). The program increases awareness among steam system operations andmanagement personnel of the benefits of insulation and assists these stakeholders in assessing insulation opportunities.

3E Plus assists the user in assessing important insulation project factors such as energy savings, installation cost, and payback period for various insulation materials and thicknesses. Users of3E Plus can estimate energy losses from uninsulated surfaces as well as potential savings from various insulation options.

The program has general data for insulationcosts by type and can analyze insulation crosssections that use several different insulation types. It also accounts for labor rates and productivity



### 27

### 28 by region, estimating how difficult the installation process will be based on general piping characteristics. Users can quickly determine theeconomic feasibility of various insulation thicknesses. Since the program also allows the user to evaluate various combinations of insulation types, 3E Plus can help the user optimize the material thicknesses within an insulation system. Download 3E Plus from the BestPractices Web site at www.eere.energy.gov/industry/bestpractices.

◆ 

### NIA’s Insulation Energy Appraisal Program (IEAP) The National Insulation Association (NIA), an ITP Allied Partner, has developed a training program that offers certification to professionals who conduct insulation appraisals or specify insulation requirements. This program is intended to provide credibility to insulation professionals and to increase consistency of the message that is presented to clients. This program has four key components:
■ Awareness Building—an important way to increase awareness of the potential cost savings from insulation projects is to effectively promote insulation appraisal as a professional service.

■ Information Gathering—determining the parts of the system that have the most attractive insulation improvement opportunities usually requires input from the plant personnel.Improving the interview techniques of insulation professionals can increase the usefulness of these assessments.

■ 3E Plus—the 3E Plus program is an important tool for insulation professionals and specifying engineers. Learning to effectively use this toolcan improve the quality of the assessment findings, presentation of recommendations, and cost-effective specification of new insulation.

■ Reporting—accurately and effectively reporting the results of an insulation assessment can significantly increase the probability that the recommendations will be implemented.

Information regarding the Insulation Energy Appraisal Program (IEAP) can be obtained from the NIA Web site at www.insulation.org.

◆ 

### Steam Tip Sheets Some improvement opportunities are available to many different systems. To increase industry awareness of several fundamental improvement opportunities, ITP has developed steam tip sheets through its BestPractices activities.

These steam tip sheets provide concise descriptions of common improvement opportunities. Because BestPractices continues to develop and identify energy improvement programs, additional tip sheets are expected. Steam tip sheets available by this Sourcebook’s publication date can be found in Appendix B. Additionally, steam tip sheets can be found on the BestPractices Web site at www.eere.energy.gov/industry/bestpractices/.


# Steam System Training

◆ 

### Steam End User Training This 1-day course covers the operation of typical steam systems and discusses methods of system efficiency improvement. The training is designed for plant personnel, such as energy managers,steam system supervisors, engineers, and equipment operators, who have steam system responsibilities in industrial and institutional plants. The course covers three key areas of potential system improvement:

■ Steam Generation Efficiency

■ Resource Utililization Effectiveness

■ Steam Distribution System Losses The course introduces the Steam System Scoping Tool and the Steam System Assessment Tool, both developed by DOE's BestPractices and uses the Steam System Survey Guide as a technical reference. The training also introduces the 3E Plus insulation appraisal software and a course example is presented that uses this software.

◆ 

### Steam Tool Specialist Qualification Training Industry professionals can earn recognition as Qualified Specialists in the use of the BestPracticesSteam Tools. DOE offers an in-depth, two-anda-half-day training for steam system specialists, including two days of classroom instruction and a written exam. Participants who complete thetraining and pass the written exam are recognized by DOE as Qualified Steam Tool Specialists, and are listed on the BestPractices Web site. Specialists can assist industrial customers in using the BestPractices Steam Tools to evaluate their steam systems.

The BestPractices Steam System Specialist Qualification training is primarily designed for steam

Improving Steam System Performance 

### Performance Improvement Opportunities

### 29specialists who are interested in becoming proficient in using the BestPractices Steam Tools. To successfully complete the Specialist Qualification Training course, a participant must understand the full suite of BestPractices Steam tools including:

■ Steam System Survey Guide

■ Steam System Scoping Tool – Accurate collection and input of data

for use with the tool – Appropriate utilization of the software – Interpretation of the software results

■ Steam System Assessment Tool – Accurate collection and input of data for

use with the tool – Development of representative system models
– SSAT limitations – Individual project identification – Development of practical methods to

accomplish the appropriate projects

■ 3E Plus – Accurate data gathering for basic

insulation related evaluations – Development of evaluation techniques

related to common insulation evaluations.

Class participants will receive a Prerequisite Test/Study Guide before attending the class. This Study Guide provides an indicator of the skill levels necessary to successfully complete the Specialist Qualification training. Completion of this Study Guide is highly recommended, but isnot a requirement to take the training. Completion of BestPractices Steam End User training is also recommended prior to participating in the Specialist Qualification training class, which covers the majority of the Specialist Qualification training prerequisites.

To learn more about the Steam System Specialist Qualification training, visit the BestPractices Web site at www.eere.energy.gov/industry/bestpractices.


# Overview of Financing Steam System Improvements

Very often, industrial facility managers must convince upper management that an investmentin steam efficiency is worth the effort. The communication of this message can often be more difficult than the actual engineering behind the concept. The corporate audience will respond more readily to an economic impact than to a discussion of Btu, pounds of steam, and efficiency ratios. By adopting a financial approach, thefacility manager relates steam efficiency to corporate goals. Collaboration with financial staff can yield the kind of proposal that is needed to convince corporate officers who have the final word about capital investments such as steam system upgrades.

Before laying out some recommendations for how to justify steam improvement projects, it is useful to understand the world as the corporate office usually sees it.

◆ 

### Understanding Corporate Priorities Corporate officers are held accountable to a chief executive, a board of directors, and an owner (or shareholders, if the firm is publicly held). It is the job of these officers to create and grow the equity value of the firm. The corporation’s industrial facilities do so by generating revenue that exceeds the cost of owning and operating the facility itself. Plant equipment—including steam system components—is an asset that must generate an economic return. The annual earnings attributable to the sale of goods produced by these assets, divided by the value of the plant assets themselves, describe the rate of return on assets. This is a key measure by which corporate decision-makers are held accountable.

Financial officers seek investments that are most certain to demonstrate a favorable return on assets. When faced with multiple investment opportunities, the officers will favor those options that lead to both the largest and fastest returns.

This corporate attitude may impose (sometimes unpleasant) priorities on the facility manager: assure reliability in production, avoid unwanted surprises by sticking with familiar technology and practices, and contribute to cost control today by cutting a few corners in maintenanceand upkeep. This may result in industrial decisionmakers concluding that steam efficiency is a “luxury” that cannot be afforded.

Fortunately, the story does not end here. What follows is a discussion of ways that industrial steam efficiency can save money and contribute to corporate goals while effectively reducing

A Sourcebook for Industry 

### Performance Improvement Opportunities

### 30 energy consumption and cutting noxious combustion emissions.

◆ 

### Measuring the Dollar Impact of Steam Efficiency Steam efficiency improvements can move to the top of the list of corporate priorities if the proposals respond to distinct corporate needs. Corporate challenges are many and varied, which in turn open up more opportunities to “sell” steam efficiency as a solution. Steam systems offermany opportunities for improvement; the particulars are shared elsewhere in this Sourcebook. Once the selections are made, the task is one of communicating the proposals in corporate financial language.

The first step is to identify and enumerate the total dollar impact of a steam efficiency measure. One framework for this is known as “life-cycle cost analysis.” These analyses capture the sum total ofexpenses and benefits associated with an investment. The result—a net gain or loss on balance— can be compared to other investment options or to the anticipated outcome if no investment is made. As a comprehensive accounting of an investmentoption, the life-cycle cost analysis for a steam efficiency measure would include projections of:

■ Search and selection costs for seeking an engineering implementation firm

■ Initial capital costs, including asset purchase, installation, and costs of borrowing

■ Maintenance costs

■ Supply and consumable costs

■ Energy costs over the economic life of the implementation

■ Depreciation and tax impacts

■ Scrap value or cost of disposal at the end of the equipment’s economic life

■ Impacts on production such as product quality and downtime.

One revelation that typically emerges from this exercise is that fuel costs may represent as much as 96% of life-cycle costs, while the initial capital outlay is only 3%, and maintenance a mere 1%. These findings may be true for boilers with a 20-year life operating at high rates of capacity utilization. Clearly, any measure that reduces fuel consumption (while not impacting reliability and productivity) will certainly yield positive financial impacts for the company. ◆ 

### Financing Steam Efficiency Improvements As with any corporate investment, there are many ways to measure the financial impact of steam efficiency investments. Some methods are more complex than others are, and proposals may use several analytical methods side-by-side. The choice of analyses used will depend on the sophistication of the presenter and the audience.
A simple and widely used measure of project economics is the payback period. This is defined as the period of time required for a project to “break even.” It is the time needed for the net benefits of an investment to accrue to the point where they equal the cost of the initial outlay. For a project that returns benefits in consistent, annual increments, the simple payback equalsthe initial investment divided by the annual benefit. Simple payback does not take into account the time value of money; in other words, it makes no distinction between a dollar earned today versus a dollar of future (and therefore uncertain) earnings. Still, the measure is easy to use and understand and many companies use simple payback for a quick “go/no-go” decision on a project. Five important factors to remember when calculating a simple payback:

■ It is an approximation, not an exact economic analysis

■ All benefits are measured without considering their timing

■ All economic consequences beyond the payback are ignored

■ Payback calculations will not always find the best solution (for the two reasons immediately above) when choosing among several project options

■ Payback does not consider the time value of money or tax consequences.

More sophisticated analyses take into account factors such as discount rates, tax impacts, thecost of capital, etc. One approach involves calculating the net present value of a project, which is defined in the equation below:

Net present value = Present worth of benefits – Present worth of costs

Another commonly used calculation for determining economic feasibility of a project is internal rate of return, which is defined as the discount rate that equates future net benefits (cash) to an

Improving Steam System Performance 

### Performance Improvement Opportunities

### 31 initial investment outlay. This discount rate can be compared to the interest rate at which a corporation borrows capital.

Many companies set a threshold (or hurdle) rate for projects, which is the minimum requiredinternal rate of return for a project to be considered viable. Future benefits are discounted at the threshold rate, and the net present worth of the project must be positive in order for the project to be a “go.”

◆ 

### Relating Steam Efficiency to Corporate Priorities Saving money should be a strong incentive for adopting steam efficiency. Still, that may not be enough for some corporate observers. The facility manager’s case can be strengthened by relating a positive life-cycle cost outcome to specificcorporate needs. Some suggestions for interpreting the benefits of fuel cost savings include the following (finance staff can suggest which ofthese approaches are best for the current corporate climate):

■ A new source of permanent capital. Reduced fuel expenditures—the direct benefit of steam efficiency—can be thought of as a new source of capital for the corporation. The investment that makes this efficiency possible will yield annual savings each year over the economic life of the improved steam system. Regardless of how the steam efficiency investment is financed—borrowing, retained earnings, or third party financing—the annual savings will be a permanent source of funds as long as the steam efficiency savings are maintained on a continuous basis.

■ Added shareholder value. Publicly held corporations usually embrace opportunities to enhance shareholder value. Steam efficiency can be an effective way to capture new value. Shareholder value is the product of twovariables: annual earnings and the price-toearnings (P/E) ratio. The P/E ratio describes the corporation’s stock value as the current stock price divided by the most recent annual earnings per share. To take advantage of this measure, the steam efficiency proposal should first identify annual savings (or rather, addition to earnings) that the proposal will generate. Multiplying that earnings increment by the P/E ratio yields the total new shareholder value attributable to the steam efficiency implementation. ■ Reduced cost of environmental compli ance. Facility managers can proactively seek to limit the corporation’s exposure to penalties related to environmental emissions compliance. Steam efficiency, as total-system discipline, leads to better monitoring and control of fuel use. Combustion emissions are directly related to fuel consumption; they rise and fall in tandem. By implementing steam efficiency, the corporation enjoys two benefits: decreased fuel expenditures per unit of production, and fewer incidences of emission-related penalties.

■ Improved worker comfort and safety. Steam system optimization requires ongoing monitoring and maintenance that yields safety and comfort benefits in addition to fuel savings. The routine involved in system monitoring will usually identify operational abnormalities before they present a danger to plant personnel. Containing these dangers precludes threats to life, health, and property.

■ Improved reliability and capacity utilization. Another benefit to be derived from steam efficiency is more productive use of steam assets. The efforts required to achieve andmaintain energy efficiency will largely contribute to operating efficiency. By ensuringthe integrity of steam system assets, the facility manager can promise more reliable plant operations. The flip side, from the corporate perspective, is a greater rate of return on assets employed in the plant.

◆ 

### Call to Action A proposal for steam efficiency implementationcan be made attractive to corporate decisionmakers if the facility manager:

■ Identifies opportunities for achieving steam efficiency

■ Determines the life-cycle cost of attaining each option

■ Identifies the option(s) with the greatest net benefits

■ Collaborates with financial staff to identify current corporate priorities (for example,added shareholder value, reduction of environmental compliance costs, and improved capacity utilization)

■ Generates a proposal that demonstrates how the steam efficiency project’s benefits will directly respond to current corporate needs.

A Sourcebook for Industry 

### Performance Improvement Opportunities

### 32 ◆ 

### SummaryIncreased awareness of the potential improvements in steam system efficiency and performance is an important step toward increasing the competitive capabilities of energy-intensive industries. Some of the useful steam resources and tools developed by BestPractices have been described in this section. Additional steam resources and tools and where to obtain them are described in the Resources and Tools section of this Sourcebook.

Improving Steam System Performance



### Performance Improvement Opportunities

### 33 This portion of the Sourcebook lists resources that can help end users increase the cost-effective performance of steam systems. The section is organized into three sections, described below:

◆ 

### Programs This section describes the U.S. Department of Energy’s Industrial Technologies Program (ITP) BestPractices activity, a national effort aimed at improving the performance of industrial steam systems. This section provides a list of associations and other organizations involved in the steam system marketplace.

◆ 

### Contacts This section provides a list of associations and other organizations involved in the steam system marketplace.

◆ 

### Resources This section provides information on books andreports, other publications, government and commercial statistics and market forecasts, software, training courses, and other sources of information that can help end users make informed steam system equipment purchase and system design decisions.


# The Industrial Technologies Program and BestPractices

◆ 

### Overview Industrial manufacturing consumes 36% of all energy used in the United States. ITP has programs to assist industry in achieving significant energy and process efficiencies. ITP develops and delivers advanced energy efficiency, renewable energy, and pollution prevention technologies and practices for industrial applications. Through an industry-driven initiative called Industries of the Future (IOF), ITPworks with the nation’s most energy- and resourceintensive industries to develop a vision of their future and roadmaps on how to achieve these visions over a 20-year timeframe. This collaborative process aligns industry goals with federal resourcesto accelerate research and development of advanced technologies identified as priorities by industry. The advancement of energy- and process-efficient technologies is complemented by ITP’s energy management best practices for immediate savingsresults. ITP’s BestPractices assists the eight Industries of the Future—aluminum, chemicals, forest products, glass, metal casting, mining, petroleum, and steel—to identify and realize their best energy efficiency and pollution prevention options from a system and life-cycle cost perspective. Through activities such as plant-wide energy assessments, implementation of emerging technologies, andenergy management of industrial systems, BestPractices delivers energy solutions for industry that result in significant energy and cost savings, waste reduction, pollution prevention, and enhanced environmental performance.

◆ 

### Plant Assessments Depending on the industry, energy can account for 10% or more of total operating costs. Energyassessments identify opportunities for implementing new technologies and system improvements.Many recommendations from energy assessments have simple payback periods of less than 18 months and can result in significant energy savings.

■ Plant-wide assessments help manufacturers develop comprehensive plant strategies to increase efficiency, reduce emissions, and boost productivity. Annual competitive solicitations offer a 50% cost share of up to $100,000 in matching funds.

■ Small- to medium-sized manufacturers canqualify for free assessments from the universitybased Industrial Assessment Centers.

◆ 

### Emerging Technologies Emerging technologies are those that result from research and development and are ready for full- scale demonstration in real-use applications. ITP recognizes that companies may be reluctant to invest capital in these new technologies, even though they can provide significant energy andprocess improvements. However, through technology implementation solicitations, ITP helps mitigate the risk associated with using new technologies that are supported by IOF partnerships.

A Sourcebook for Industry 

### Where to Find Help



# Section 3: Where to Find Help

### 34 By sharing implementation and providing thirdparty validation and verification of performance data, the energy, economic, and environmentalbenefits can be assessed to accelerate new technology to acceptance.

◆ 

### Energy ManagementITP encourages manufacturers to adopt a comprehensive approach to energy use that includes assessing industrial systems and evaluating potential improvement opportunities. Efficiency gains in compressed air, motor, process heating, pumping, and steam systems can be significant and usually result in immediate energy and cost savings. ITP offers software tools and training in a variety of system areas to help industry become more energy and process efficient, reduce waste, and improve environmental performance.

◆ 

### Allied Partnerships Allied Partners are manufacturers, associations, industrial service and equipment providers, utilities, and other organizations that voluntarily work with ITP. Allied Partners seek to increase energy efficiency and productivity for those industries that participate in endorsing and promoting ITP programs, products, and services.

Allied Partnerships help ITP achieve industrial energy efficiency goals by extending delivery channels through the partners’ existing networks.In turn, partners realize benefits, such as achieving their own corporate, institutional, or plant goals and objectives by expanding services to customers and suppliers. Allied Partners also gain access to technical resources, such as software, technical publications, and training; and they can gain recognition as leaders in the implementation of energy-efficient technologies and practices. For more on Allied Partnerships, contact the EERE Information Center at 877-337-3463.

◆ 

### Technical Resources ITP offers a variety of resources to help industry achieve increased energy and process efficiency, improved productivity, and greater competitiveness.

EERE Information Center. The EERE Information Center fields questions on EERE products and services including those focused on industrial energy efficiency. They can answer questions about industrial systems such as compressed air, motors, process heating, and steam. The EEREInformation Center can be the first stop in finding out what’s available from EERE and ITP. Contact the EERE Information Center at 877-337-3463 or www.eere.energy.gov/informationcenter.

ITP and BestPractices Web Sites. The ITP and BestPractices Web sites offer a large array of information, products, and resources to assist manufacturers who are interested in increasing the efficiency of their industrial operations. You can gain access to Web pages for the eight Industries of the Future, learn about upcoming events and solicitations and much more through the ITP site. Visit the ITP site at www.eere.energy.gov/industry.

The BestPractices site offers case studies of companies that have successfully implemented energy efficient technologies and practices, software tools, tip sheets, training events, and solicitations for plant assessments. You can see these and other resources at www.eere.energy.gov/industry/bestpractices.

Industrial Energy Savers Web site. Manufacturers will find a number of resources on this site to implement industrial energy efficiency projects and see immediate savings. Access this site at www.eere.energy.gov/consumerinfo/industry.

◆ 

### TrainingTraining sessions in industrial systems improvements using ITP software tools are offered periodically through Allied Partners. Visit the BestPractices Web site for more information at www.eere.energy.gov/industry/bestpractices.

◆ 

### Software ToolsITP and its partners have developed several software tools for systems improvements to help you make decisions about implementing efficient practices in your manufacturing facilities.

• AirMaster+ provides comprehensive information on assessing compressed air systems, including modeling, existing and future system upgrades, and evaluating savings and effectiveness of energy efficiency measures.

• An energy-efficient motor selection and management tool, MotorMaster+ 4.0 software, includes a catalog of over 20,000 AC motors. Version 4.0 features motor inventory management tools, maintenance log tracking, efficiency analysis, savings evaluation, energy accounting, and environmental reporting capabilities.

Improving Steam System Performance 

### Where to Find Help

### 35 • The NOx and Energy Assessment Tool (NxEAT) helps plants in the petroleum refining and chemical industries assess and analyze NOx emissions and how the application of energy efficiency improvements can reduce NOx. Perform "what-if" analyses to optimize andselect the most cost-effective methods for reducing NOx from systems such as fired heaters, boilers, gas turbines, and reciprocating engines.

• The Process Heating Assessment and Survey Tool (PHAST) provides an introduction to process heating methods and tools toimprove thermal efficiency of heating equipment. Use the tool to survey process heating equipment that uses fuel, steam, or electricity,and identify the most energy-intensive equipment. You can also perform an energy (heat) balance on selected equipment (furnaces) to identify and reduce non-productive energy use. Compare performance of the furnace under various operating conditions and test "what-if" scenarios.

• The Pumping System Assessment Tool (PSAT) helps industrial users assess the efficiencyof pumping system operations. PSAT uses achievable pump performance data from Hydraulic Institute standards and motor performance data from the MotorMaster+ database to calculate potential energy and associated cost savings.

◆ 

### Newsletters

• The Industrial Technologies Program E-Bulletin is a monthly e-mail update that spotlights technologies, significant project developments, and program activities; new ITP and BestPractices products; training and events; Web updates; and solicitations. The E-Bulletinprovides readers with links to source information on the ITP, BestPractices, and IAC Web sites. To subscribe, go to: www.eere.energy.gov/ industry/resources/itp_ebulletin.html.

• Energy Matters is a bimonthly newsletter written by ITP that provides news, technical tips, and case studies. Energy Matters informs industrial end users of energy efficiency opportunities, technical issues, new products and services, and events related to process heating systems and other industrial utilities such as motor, steam, and compressed air systems. To subscribe, contact the EERE Information Center (877-337-3463) or subscribe online at: www.eere.energy.gov/industry/bestpractices.
A Sourcebook for Industry 

### Where to Find Help

Software: DOE’s Steam System Tool Suite helps you tap into potential savings in your facility, by evaluating and identifying steam system improvements. Steam System Scoping Tool —This tool is designed to helpsteam system energy managers and operations personnel perform initial self-assessments of their steam systems. This toolwill profile and grade steam system operations and management, and will help you to evaluate your steam system operations against best practices. Steam System Assessment Tool (SSAT 2.0.0) —This tool allows users to assess potential savings from individualized steam system improvements. Users input data about their plant's conditions, and the SSAT generates results detailing the energy, cost, and emissions savings that could be achieved through 16 different improvements.

3E Plus Version 3.2—This program calculates the most economical thickness of industrial insulation for user input operating conditions. You can make calculations using the built-in thermal performance relationships of generic insulation materials or supply conductivity data for other materials. Training: Steam Tool Specialist Qualification Training —Industry professionals can earn recognition as Qualified Specialists in the use of the BestPractices Steam Tools. DOE offers an in-depth 2-1/2 day training for steam system special ists, including 2 days of classroom instruction and a written exam. Participants who complete the training and pass the written exam are recognized by DOE as Qualified Steam Tool Specialists. Specialists can assist industrial customers in using the BestPractices Steam Tools to evaluate their steam systems.

Newsletter: Steaming Ahead is a bimonthly e-mail newsletter published by the Alliance to Save Energy that describes the activities and information products of the BestPractices Steam effort. BestPractices Steam outreach and promotion is performed by the Alliance to Save Energy. Steaming Ahead promotes best-in-class practices and technology applications in steam system design and management. Additional information

on Steaming Ahead can be found at: www.steamingahead.org.
Case Studies: Steam Case Studies provide practical examples of successful steam system improvement projects. Typically, these case studies describe how a facility assessed its steam system, then identified opportunities to improve its operation and/or performance and implemented one or more of these opportunities. Discussion of successful improvement projectscan reduce the uncertainty associated with making steam system improvements. Case studies also increase awareness of the systems approach that is often an essential part of any successful performance or efficiency improvement. Documented steam case studies are available from the BestPractices Web site at www.eere.energy.gov/industry/bestpractices. 

### DOE Steam-Specific Resources

### 36 

# Directory of Contacts

Information on improving the performance of industrial energy systems is available from several resources. To improve the profitability of U.S. industry, ITP’s BestPractices offers many resources for steam system management. These resources complement Industries of the Future technology development programs, which address other industrial systems, such as motor, compressed air, combined heat and power, and process heating, in addition to efforts by the Industrial Assessment Centers. Collectively, these efforts assist industryin adopting near-term and long-term energyefficient practices and technologies. For assistance in these areas, contact:



### U.S. Department of Energy Industrial Technologies Program BestPractices Steam Room 5-F-065, MS EE-2F 1000 Independence Avenue, SW Washington, DC 20525 Phone: 877-337-3463 www.eere.energy.gov/industry

For specific information regarding steam systems, including assistance in locating steam system specialists and equipment vendors, BestPractices Steam provides an excellent set of helpful resources. Together with industrial end users, equipment suppliers, and resource organizations, BestPracticesSteam helps industry stay competitive and promotes the comprehensive upgrade of industrial steam sys tems.



### Alliance to Save Energy 1200 18th Street, NW, Suite 900 Washington, DC 20036 Phone: 202-857-0666 Fax: 202-331-9588 www.ase.org
The Alliance to Save Energy is a nonprofit coalition of prominent business, government, environmental, and consumer leaders who promote the efficient and clean use of energy worldwide to benefit the environment, the economy, and national security. 

### American Boiler Manufacturers Association (ABMA) 4001 North 9th Street, Suite 226 Arlington, VA 22203-1900 Phone: 703-522-7350 Fax: 703-522-2665 www.abma.com

ABMA is a trade association of manufacturers of boilers, related fuel-burning equipment, users ofboiler and boiler-related equipment, and companies that provide products and services to the boiler industry.

The ABMA Bookstore is a one-stop source for boiler industry information. Find industry standards, technical references, and more from ABMA, Underwriters Laboratories, and many other publishers.



### Association of Energy Engineers (AEE) 4025 Pleasantdale Road, Suite 420 Atlanta, GA 30340 Phone: 770-447-5083 Fax: 770-446-3969 www.aeecenter.org

AEE is a membership organization of over 8,000 professionals in the energy efficiency, utility deregulation, facility management, plant engineering, and environmental compliance fields. AEE offers a variety of outreach programs including technical seminars, conferences, publications, and certification programs.



### Association for Facilities Engineering (AFE) 8160 Corporate Park Drive, Suite 125 Cincinnati, OH 45242 Phone: 513-489-2473 Fax: 513-247-7422 www.afe.org

AFE provides education, certification, technical information, and other relevant resources for plant and facility engineering, operations, and maintenance professionals worldwide.



### Boiler Room/Go-Steam Web sites An online community for commercial and industrial boiler operators and engineers.This site contains boiler company profiles, a careercenter for steam industry professionals, a classified section for boiler/steam equipment, and a discussion board. See www.boilerroom.com and www.gosteam.com.

Improving Steam System Performance 

### Where to Find Help

### Council of Industrial Boiler Owners (CIBO) 6035 Burke Centre Parkway, Suite 360 Burke, VA 22015 Phone: 703-250-9042 Fax: 703-239-9042 www.cibo.org

CIBO provides information and advocacy toachieve solutions to industrial energy, environmental, and legislative issues and policies. Objectives of CIBO include: 1. Information exchange among members, government, and the public concerning policies, laws, and regulations that affect industrial energy systems. 2. Technically sound, equitable, cost-effective laws and regulations. 3. Improved reliability and cost-effectiveness of industrial energy systems.



### National Association of Power Engineers (NAPE) 1 Springfield Street Chicopee, MA 01013 Phone: 413-592-6273 www.powerengineers.com

NAPE is a professional association for power engineers. NAPE was established in 1879 and provides education and resources on power and energy engineering.



### National Insulation Association (NIA) 99 Canal Center Plaza, Suite 222 Alexandria, VA 22314 Phone: 703-683-6422 Fax: 703-549-4838 www.insulation.org

NIA is a service organization that promotes the general welfare of the commercial and industrial insulation and asbestos abatement industries andworks to improve the service to the general public performed by the commercial and industrial insulation and asbestos abatement industries.



### North American Insulation Manufacturers Association (NAIMA) 44 Canal Center Plaza, Suite 310 Alexandria, VA 22314 Phone: 703-684-0084 Fax: 703-684-0427 www.naima.org NAIMA is a trade association of North American manufacturers of fiberglass, rock wool, and slag wool insulation products. NAIMA concentrates its efforts on promoting energy efficiency and environmental preservation through the use of fiberglass, rock wool, and slag wool insulation products, while encouraging safe production and use of these products.



### STEAM-LISTThe STEAM-LIST is a discussion forum that promotes the exchange of information, problem solving, and discussion of steam generators, piping, and equipment. Included among the components and issues that are discussed are boilers, boiler feed pumps, water treatment, corrosion andscaling, valves, PRVs, traps, turbines, flow metering, heating coils, condensate pumps, districtheating, and system modeling. This list is intended to promote practical discussions, rather than theoretical or academic discussions.

Subscription information can be obtained by contacting: listproc@lists.cc.utexas.edu.



# Resources and Tools

Note: The descriptions accompanying the following sources have generally been taken directly from the publisher/author/developer. Inclusion of these sources does not imply endorsement by the U.S. Department of Energy.

Several other resources are available that describe current tools, technologies, and practices that can help improve steam system operating efficiency and performance. Many of these resources are intended to increase awareness of the benefits of energy improvement projects and to identify where the industry professional can go for more help.



### Armstrong International, Inc. 816 Maple Street Three Rivers, MI 49093 269-273-1415 www.armintl.com

Handbook N101—Steam Conservation Guidelines for Condensate Drainage Description: This Handbook summarizes general principles of installation and operation of steam

A Sourcebook for Industry 

### 37 Where to Find Help



## Bookstraps. It also includes Recommendation Charts which summarize findings on which type of trap will give optimum performance in a given situation and why. 

### ASHRAE 1791 Tullie Circle, NE Atlanta, GA 30329 800-527-4723 www.ashrae.org

ASHRAE Handbook of HVAC Systems and Equipment, 2000 Description: Complete guide to steam systems design and equipment.



### Association for Facilities Engineering (AFE) 8160 Corporate Park Drive, Suite 125 Cincinnati, OH 45242 513-489-2473 www.afe.org

Boiler Plant and Distribution Optimization Manual Description: Guide for boiler and plant operators to optimize the efficiency of their boilers and distribution systems.



### Babcock and Wilcox 20 South Van Buren Avenue Barberton, OH 44203-0351 330-753-4511 www.babcock.com

Steam: Its Generation and Use, 40th Edition Description: This book is intended to help design, procure, construct, maintain, and/or operate equipment in a way that will provide reliable performance.



### GE Betz 4636 Somerton Road Trevose, PA 19053-6783 215-355-3300 www.gewater.com

Handbook of Industrial Water Conditioning, Ninth Edition Prepared by: Betz Laboratories Inc. Description: This handbook presents detailed information on external treatment: boiler and cooling water systems, air conditioning, refrigeration and total energy systems, chemical treatment feeding and control, and problems encountered in special industrial cases. 

### Boiler Efficiency Institute P.O. Box 2255 Auburn, AL 36831-2255 800-669-6948 www.boilerinstitute.com

Steam Efficiency Improvement Description: An introductory text for establishing a program for reducing losses in the use of steam. The text is divided into three areas: steam transmission, steam consuming processes, and condensate return systems.



### CANMET Energy Technology Centre 1 Haanel Drive Ottawa, Ontario Canada K1A 1M1 613-996-8693 www.nrcan.gc.ca/es/etb/cetc/cetchome.htm

An Energy Efficiency and Environment Primer for Boilers and Heaters Prepared by: Federal Industrial Boiler Program, CANMET Energy Technology Centre Description: This guide is intended to provide a basic discussion of combustion processes, their emissions, and techniques for reducing energy consumption and environmental emissions. ISBN: 0777895366



### Council of Industrial Boiler Operators (CIBO) 6035 Burke Centre Parkway, Suite 360 Burke, VA 22015 703-250-9042 www.cibo.org

Energy Efficiency Handbook Description: The Energy Efficiency Handbook was prepared to help owners and operators get the best and most energy-efficient performance out of their boiler systems. Some of the handbook chapters include Water Treatment, Boilers, Controls, Heat Recovery, Energy Auditing, and Steam Systems.



### Energy Institute Press 3969 Lantern Drive Wheaton, MD 20902 301-946-1196 www.energybooks.com

Improving Steam System Performance 

### 38 Where to Find HelpA Sourcebook for Industry 

### 39 Energy Efficiency Manual Author: Donald R. Wulfinghoff Description: A comprehensive treatment of energy efficiency applications in industrial, commercial, and residential settings. Industrial boiler operators will be interested in Section 1, “Boiler Plant,” which devotes 225 pages solely to steam systems. Dozens of tips are provided, each with an assessment oftheir potential for savings, rate of return, reliability, and ease of initiation. ISBN: 0965792676



### The Fairmont Press 700 Indian Trail Lilburn, GA 30047 770-925-9388 www.fairmontpress.com

Efficient Boiler Operations Source Book, Fourth Edition Authors: F. William Payne and Richard E. Thompson Description: Reviews the fundamentals of boiler combustion and the factors that affect boiler efficiency. This book is intended for operators and supervisors of boiler plants. ISBN: 01353226885

Energy Management Handbook Author: Wayne C. Turner Description: This book discusses steam and condensate systems, waste heat recovery, co-generation, and industrial insulation. ISBN: 013728098X

Handbook of Energy Audits, Fourth Edition Author: Albert Thumann Description: Contains information on boilers, steam traps, insulation, and a chapter on computer software for energy audits. ISBN: 0139752021

Plant Engineer’s and Manager’s Guide to Energy Conservation, Seventh Edition Author: Albert Thumann Description: Provides information on steam tracing, steam generation using waste heat recovery, steam trap maintenance, cogeneration, the transition from energy audits to industrial assessment, a review of industrial operations and maintenance energy measures, and an integrated approach to achieving energy cost savings at a corporate headquarters. ISBN: 0130207381

Stationary Engineering Handbook Author: K. L. Petrocelly, SMA/CPE Description: A book that discusses steam generation and water treatment from the operating engineer’s perspective. The Steam Trap Handbook Author: James F. McCauley Description: This book is intended for engineers and technicians to help them optimize the performance of their steam systems by focusing on steam traps. This book discusses proper selection and sizing, application, operation, and maintenance of steam traps.



### International District Energy Association 125 Turnpike Road, Suite 4 Westborough, MA 01581-2841 508-366-9339 www.districtenergy.org

District Heating Handbook, Fourth Edition Description: A guide for engineers to understand district heating and how best to use it.



### John Wiley & Sons 111 River Street Hoboken, NJ 07030-5774 201-748-6000 www.wiley.com

Handbook of Energy Systems Engineering Production and Utilization Author: Leslie Wilbur (Editor) Description: This book covers all aspects of energy system engineering from a user’s perspective. It presents a holistic approach to understanding these systems from fuels to end-use technologies for mechanical and electric production and utilization in industry today. The extensive list of references provided are invaluable to anyone interested in energy production and utilization. Publication, 1985.



### Krieger Publishing Company P.O. Box 9542 Melbourne, FL 32902-9542 321-724-9542 www.krieger_publishing.com

Handbook of Thermal Insulation Design Economics for Pipes and Equipment Authors: William C. Turner and John F. Malloy Description: This handbook discusses topics such as heat transfer, insulation materials properties, selection/application/installation, and energy savings. 

### Where to Find HelpImproving Steam System Performance 

### 40 Marcel Dekker, Inc. 270 Madison Avenue New York, NY 10016-0602 212-696-9000 www.dekker.com

Steam Plant Calculations Manual Author: V. Ganapathy Description: Provides solutions to nearly 200 practical questions related to the planning, design, operation, and maintenance of steam plant systems.



### McGraw-Hill 1221 Avenue of the Americas New York, NY 10020 212-512-2000 www.bookstore.mcgraw-hill.com

Marks Standard Handbook for Mechanical Engineers Authors: Eugene Avallone and Theodore Baumeister, III (Editors) Description: Provides descriptions of different heat distribution systems including low-pressure steam systems. ISBN: 0070049971

A Practical Guide to Steam Turbine Technology Author: Heinz P. Bloch Description: This book is written for plant, mechanical, design, and maintenance engineers, and will assist end users with selecting, operating, and maintaining steam-driven systems. It includes design and manufacturing data for steam turbines and compressors, as well as the other operational components. ISBN : 0070059241

Shreve's Chemical Process Industries, Fifth Edition Author: G. T. Austin Description: The book provides an overview of the chemical processing of raw materials into useful and profitable products. It provides process descriptions and diagrams for many chemical processing operations.

A Working Guide to Process Equipment Authors: Norman P. Lieberman and Elizabeth T. Lieberman Description: Explains the basic technical issues that need to be known to trouble shoot process equipment problems. Provides diagnostic tips, worked out calculations, practical examples, and illustrations. 

### Nalco Company 1601 West Diehl Road Naperville, IL 60563-1198 877-813-3523 www.nalco.com

Nalco Guide to Boiler Failure Analysis Authors: Robert D. Port and Harvey M. Herro Description: This book is a comprehensive field guide to boiler system failures. It is intended to aid in-plant detecti on and diagno sis. Correction procedures can usually be specified once the cause of system failures has been determined.

Nalco Water Handbook, Second Edition Author: Frank N. Kemmer (Editor) Description: This reference discusses the use ofwater and steam in water treatment unit operations, the use of water and steam in a number of major process industries, and specialized water treatment technologies in boilers and other systems.



### Pennwell Publishing 1421 South Sheridan Road Tulsa, OK 74112 918-835-3161 www.pennwell.com

Petrochemicals in Nontechnical Language, Third Edition Authors: Donald L. Burdick and William L. Leffler Description: Provides an overview of the key processes and operations in the petrochemicals industry.

Petroleum Refining in Nontechnical Language, Third Edition Author: William L. Leffler Description: Provides an overview of the key processes and operations in the petroleum refining industry for professionals in finance and marketing.



### Prentice Hall/Pearson Education One Lake Street Upper Saddle River, NJ 07458 800-382-3419 www.prenhall.com

Energy Analysis of 108 Industrial Processes Authors: Harry Brown, Bernard Hamel, and Bruce Hedman Description: A reference for identifying the quantity and quality of industrial waste energy, which can be 

### Where to Find HelpA Sourcebook for Industry 

### 41 economically practical to recover. Presents detailed heat and material balances developed from the process flow diagrams for 108 industrial processes.

Handbook of Industrial Power & Steam Systems Author: Paul Garay Description: Describes the design and operation features of industrial power plants, considering such aspects as environmental concerns, basic energy and steam, electrical systems, heat recovery, energyconservation, codes and standards, and information sources. Publication, 1995. ISBN: 0131474146



### Spirax Sarco Application Engineering Department 1150 Northpoint Boulevard Blythewood, SC 29016 803-714-2000 www.spirax-sarco.com

Hook-Ups—Design of Fluid Systems Description: The Hook-Up Book is intended to serveas a reference in the design, operation, and maintenance of steam, air, and liquid systems. The book is alearning tool to teach engineers how to design productive steam systems efficiently and cost effectively.

Steam Utilization—Design of Fluid Systems Description: The Steam Utilization Book is intended to serve as a reference in steam fundamentals to the most efficient use of steam heat content. The book describes proper steam trapping, controls, and condensate recovery.



### TAPPI Press 15 Technology Parkway South Norcross, GA 30092 800-332-8685 www.tappi.org

Energy Cost Reduction in the Pulp and Paper Industry Prepared by: Paprican (Canada) Description: Provides an overview of cost reduction opportunities available in pulp and paper plants.



### TLV Company Ltd. 13901 South Lakes Drive Charlotte, NC 28273-6790 704-597-9070 www.tlv.com

Condensate Drainage and Recovery Description: This handbook provides a practical introduction to draining condensate from equipment and returning it to the boiler system. Publication, 1997. Efficient Use of Process Steam Description: This handbook provides a practical introduction to steam properties, and a basic awareness of how steam can be successfully and beneficially used in industry. Publication, 1996.

Steam Trapping Principles Description: This handbook explains the technology of steam trapping, and provides data to correctly select and install steam traps for the benefit of maximum plant efficiency.



### Yarway Corporation/Tyco Valve & Controls 9700 West Gulf Bank Road Houston, TX 72040 713-466-1176 www.yarway.com

Industrial Steam Trapping Handbook Description: Focuses on good steam piping/ system/application practices. Includes extensive information on different steam trap technologies, condensate line sizing, and steam trap testing techniques.



### American Boiler Manufacturers Association (ABMA) 4001 North 9th Street, Suite 226 Arlington, VA 22203-1900 703-522-7350 www.abma.com

ABMA provides a wide range of guides, manuals, and other publications on boiler operations and maintenance.



### American Gas Association (AGA) 400 North Capitol Street, NW, Suite 450 Washington, DC 20001 202-824-7000 www.aga.org

Boiler NO x Control Field Manual, 1994 Description: This manual provides an applicationsreference and guidebook to assist gas utility marketing personnel in working with industrial customers to address the control oxides of nitrogen. 

### Where to Find Help



## Other Publications (Guides, Manuals, and Standards)

### American National Standards Institute (ANSI) Fluid Control Institute of America, ANSI 25 West 43rd Street New York, NY 10036 212-642-4900 www.ansi.org

ANSI/Fluid Control Institute 69-1-1989 (revised 1994) Description: Pressure ratings for steam traps.

ANSI/Fluid Control Institute 85-1-1994 Description: Standard for production testing of steam traps.

ANSI Fluid Control Institute 87-1-1994 Description: Classifications and operating principles of steam traps.

Fluid Control Institute 97.1 Description: Standard for production testing of secondary pressure drainers (condensate return pumps).



### American Society of Mechanical Engineers (ASME) Three Park Avenue New York, NY 10016-5990 800-843-2763 www.asme.org

ANSI/ASME PTC 39.1, Performance Testing Description: Reviews all the necessary information to conduct performance tests on steam traps for efficient use of plant steam.

ASME B31.1 Power Piping Code 1995 Edition Description: Code of standards for pressure piping.

ASME Boiler/Pressure Vessel Code Description: Construction specifications associated with boilers and their operation.

Consensus on Operating Practices for the Control of Feedwater and Boiler Water Chemistry in Modern Industrial Boilers (CRTD-Vol. 34) Description: Guidelines aimed at minimizing boiler deposition.

A Practical Guide to Avoiding Steam Purity Problems in the Industrial Plant (CRTD-Vol. 35) Description: Guidelines aimed at avoiding steam purity related problems. 

### Armstrong International, Inc. 816 Maple Street Three Rivers, MI 49093 269-273-1415 www.armintl.com

Armstrong Service Guide Bulletin–301 Description: Steam trap installation and maintenance.

Chart 1101 - A Quick Way to Find How Much Steam You Need to Heat Water Description: Chart showing amount of steam and the boiler horsepower required to heat water.

Chart 1121 - How to Size Condensate Return Lines Description: Sizing condensate return lines presents several problems that differ from those of sizing steam or water lines. The most significant is handling flash steam. The chart contains formulas to size condensate lines and return line capacity data.

Installation and Testing of Inverted Bucket Steam Traps–Bulletin - 307 Description: Steam trap testing for Inverted Bucket traps.

Steam Trap Testing Guide for Energy Conservation Description: Trap testing for all trap styles.



### ASTM International 100 Barr Harbor Drive West Conshohocken, PA 19428-2959 610-832-9585 www.astm.org

Annual Book of Standards 2004, Section Four, Volume 04.06, “Thermal Insulation: Environmental Acoustics”. Description: Features specifications that establishproperty requirements for various types of insulation. Also included are tests, practices, and guides that call out procedures for the measurement of insulation properties as well as installation.



### British Standards Institution (BSI) 389 Chiswick High Road London W4 4AL United Kingdom +44 (0)20 8996 7001 www.bsi.org.uk

Improving Steam System Performance 

### 42 Where to Find HelpA Sourcebook for Industry 

### 43 Recommendations for Treatment of Water for Steam Boilers and Water Heaters (BS 2486:1997) Description: The standard gives recommendations for the control of waterside conditions in steamboilers and water heaters. It also includes information on the preparation of feedwater required for these systems.



### National Board of Boiler and Pressure Vessel Inspectors 1055 Crupper Avenue Columbus, OH 43229 614-888-8320 www.nationalboard.org

National Board Inspection Code, ANSI/NB-23 National Board of Boiler and Pressure Vessel Inspectors Description: The purpose of the National Board Inspection Code is to “Maintain the integrity of pressure retaining items after they have been placed into service by providing rules for inspection, repair, and alteration...”



### National Insulation Association (NIA) 99 Canal Center Plaza, Suite 222 Alexandria, VA 22314 703-683-6422 www.insulation.org

National Commercial and Industrial Insulation Standards Description: This is a national standard for designing, specifying, and installing thermal mechanical insulation for commercial and industrial pipe, equipment, vessels, and ducting systems.



### Plant Support & Evaluations, Inc. 282 Shellstone Court Naples, Florida 34119 888-615-3559 www.plantsupport.com

Steam System Specialist Level One - Training Manual Description: The training manual covers all aspects of the steam system. It provides the necessary basicinformation on steam, heat transfer, boilers, piping, heat exchangers, insulation, and steam traps.

Steam System Specialist Level Two - Training Manual Description: The training manual provides more detail on certain aspects of the steam system. Areas of coverage include steam generation,steam turbines, desuperheaters, steam accumulators, piping, expansion, heat transfer, process control, and condensate recovery. 

### Process Industry Practices 3925 West Braker Lane (R4500) Austin, TX 78759 512-232-3041 www.pip.org

Process Industry Practices (PIP) is a consortium ofprocess industry owners and engineering construction contractors who serve the industry. PIP publishes documents called "Practices." These Practices reflect a combination of company engineering standards in many engineering disciplines. Specific Practices include design, selection and specification, and installation information.



### Spirax Sarco Application Engineering Department 1150 Northpoint Boulevard Blythewood, SC 29016 803-714-2000 www.spirax-sarco.com

Spirax Sarco Products, Applications and Systems for the Steam and Condensate Loop “Wall Chart” Description: Wall chart of a total steam system, showing steam generation, distribution, end-use and recovery guidelines.

Spirax Sarco Specification Guide and Designers Notes Description: Guideline specification and designer note requirements for industrial, HVAC, and clean steam systems.

Steam Distribution. Technical Reference Guide (TR-GCM-03) Description: This guide looks at the distribution of dry saturated steam as a conveyor of heat energyto the point of use, for either process heat exchange applications or space heating. It covers the issues associated with the implementation of an efficient steam system.



### TAPPI Press 15 Technology Parkway South Norcross, GA 30092 800-332-8685 www.tappi.org



### Paper Machine Steam and Condensate Systems Description: Provides information to solve dryingrelated problems and gives a basic understanding of paper machine steam and condensate systems. 

### Where to Find Help

### United Kingdom Energy Efficiency Action Energy Web site Good Practice Guides +44 (0)08 0058 5794 www.actionenergy.co.uk

The Action Energy site provides an extensive list of publications on industrial energy efficiency including the following Good Practices Guides:



### Guidance for Coal-Fired Boiler Operation Description: Guidelines for boiler operation for boilers fueled by coal.



### Guidance for Gas-Fired Boiler Operation Description: Guidelines for boiler operation for boilers fueled by gas.



### Guidance for Oil-Fired Boiler Operation Description: Guidelines for boiler operation for boilers fueled by oil.



### U.S. Army Corps of Engineers 441 G Street, NW Washington, DC 20314-1000 202-761-0001 www.usace.army.mil

Industrial Water Treatment Procedures, PWTB 420-49-5 Description: Guide for boiler plant operators to properly set up, maintain, and control boiler system water chemistry. Applies to boiler systems operating below 600 psi. Includes guidelines for water treatment for other HVAC systems.



### U.S. Department of Energy Information Bridge P.O. Box 62 Oak Ridge, TN 37831 888-293-6498 www.osti.gov/bridge

Guide to Low-Emission Boiler and Combustion Equipment Selection Description: Guide presents topics pertaining to industrial, commercial, and institutional (ICI) boilers. Background information about varioustypes of commercially available boilers is provided, along with discussions about the fuels that they burn and the emissions that they produce. Use of the guide is primarily intended for those involved in either expanding current steam or hot water generating capacity or developing new capacity. Document reference: ORNL/TM-2002/19. Guide to Combined Heat and Power Systems for Boiler Owners and Operators Description: This guide is a resource to help industry evaluate the viability of cogeneration for new or existing ICI boiler installations. Information in the guide focuses on technical, economic, and regulatory issues that boiler owners and operators should consider during the planning phase of any CHP project. In addition, the guide identifiesmany of the potential benefits and possible barriers to successful implementation of cogeneration technology. The guide was developed with the American Boiler Manufacturers Association (ABMA) and the Council of Industrial Boiler Owners (CIBO). Document reference: ORNL/TM-2004/144.



### U.S. Environmental Protection Agency Ariel Rios Building 1200 Pennsylvania Avenue, NW Washington, DC 20460 202-272-0167 www.epa.gov

Wise Rules Tool Kit Description: Rules and measures for estimating potential energy, cost, and greenhouse gas emissions savings with information on boilers, steam systems, furnaces, process heating, waste heat recovery, cogeneration, compressed air systems, and process cooling.



### Armstrong International, Inc. 816 Maple Street Three Rivers, MI 49093 269-273-1415 www.armintl.com

Armstrong Coil Sizing Software Developer: Armstrong International Description: Coil sizing and selection instructions for specific applications.

Armstrong Humidifier Sizing Software Developer: Armstrong International Description: Steam humidifier sizing and selection instructions for specific applications.

Armstrong Preventative Maintenance APM+ Software Developer: Armstrong International Description: Pressure Reducing Valve (PRV) sizing and selection instructions for specific applications.

Improving Steam System Performance 

### 44 Where to Find Help



## SoftwareArmstrong PRV Sizing Software Developer: Armstrong International Description: PRV sizing and selection instructions for specific applications.

Armstrong Steam Eye Software Developer: Armstrong International Description: Software designed to constantly monitor steam traps in a system.

Armstrong Trap Sizing Software Developer: Armstrong International Description: Steam trap sizing and selection instructions for specific applications.



### ChemicaLogic Corporation 99 South Bedford Street, Suite 207 Burlington, MA 01803 781-425-6738 www.chemicalogic.com

SteamTab Software Developer: ChemicaLogic Corporation Description: SteamTab is a tool designed for steam property users in the scientific, engineering, plant operation, and educational communities.SteamTab uses fundamental equations to calculate all steam properties with interpolation or curve fits to raw steam data. SteamTab products support spreadsheet applications.



### Conserv-It Software 13000-F York Road, #116 Charlotte, NC 28278 704-841-9550 www.conserv-it.com

SteamWorks Pro Developer: Conserv-It Software, Inc. Description: This software assists in tracking steam trap maintenance efforts.



### Control Dynamics, Inc. 201 Wylderose Drive P.O. Box 509 Midlothian, VA 23113 804-858-5800 www.control-dynamics.com

Boiler Control Package Tool Developer: Licensed by Fisher-Rosemount Performance Solutions Description: The Boiler Control Package is a preconfigured control strategy for use with control systemsfor steam generators; i.e., boilers, heat recovery generators, and thermal oxidizers. Controls include the water side for single or three-element drum level controls, combustion controls for parallel metering and cross-limiting of one or more fuels, with oxygentrim. Steam header pressure controls are included, as well as a simulation for training.



### EPD 14 Hayes Street Elmsford, NY 10523 800-892-8926 www.epdtech.com

DataTemp 2 Software Developer: EPD Description: DataTemp 2 Software records, stores and graphs temperature data over time. For maintenance operations and process monitoring and control, temperature trend data is critical. If that data is in a form you can’t use, you havea problem. DataTemp 2 provides a simple solution. Using an EPD PM infrared for input and your computer as a data logger and recorder, DataTemp 2 lets you take accurate temperature measurements at programmable time intervals.



### Field Data Specialists, Inc. 6917 Stennis Blvd. Pascagoula, MS 39581 800-932-9543 www.trapbase.com

TrapBase97 for Windows Software Developer: Field Data Specialists, Inc. Description: TrapBase was designed as a field tool to assist in developing a systematic steam system program. The software has features for data entry, directed surveys, field reporting, maintenance work orders/history, field data analysis, and savings results analysis. Existing data from other softwareor from spreadsheets can be imported into TrapBase. A version of the software was written to be used with the TrapTech Palm PC.



### Honeywell Corporation 11 West Spring Street Freeport, IL 61032 800-343-0228 www.iac.honeywell.com

Turbo Economic Load Allocation Developer: Honeywell Corporation Description: Calculates optimum loading for all boilers at all possible steam loads.

A Sourcebook for Industry 

### 45 Where to Find HelpImproving Steam System Performance 

### 46 Linnhoff March Targeting House Gadbrook Park Northwich, Cheshire CW9 7U3 United Kingdom +44 (0)1606 815100 www.linnhoffmarch.co.uk

PROSTEAM Software Developer: Linnhoff March Description: PROSTEAM is an engineering add-in model for a Microsoft Excel spreadsheet. It provides steam and water thermodynamic and transport property calculations, and steam utility systems modeling.



### National Institute of Standards and Technology 100 Bureau Drive, Stop 3460 Gaithersburg, MD 20899-3460 301-975-6478 www.nist.gov

NIST/ASME Steam Properties Developer: National Institute of Standards and Technology Description: Database of steam and water thermodynamic properties.



### Nelson & Roseme, Inc. P.O. Box 30024 Walnut Creek, CA 94598 925-280-0327 www.nelson-roseme.com

VisualMesa Developer: Nelson & Roseme, Inc. Description: First principles model for complicated energy systems.



### Ogontz Corporation 2835 Terwood Road Willow Grove, PA 19090 800-523-2478 www.ogontz.com

Ogontz Energy Savings Potential Developer: Ogontz Corporation Description: This software calculates the dollars that can be saved using steam controls and traps in an existing facility or new construction project. The software provides cost savings information for unit heaters, winterization steam tracing, temperature control of traced process piping, and other temperature control applications. 

### Plant Support & Evaluations, Inc. 282 Shellstone Court Naples, Florida 34119 888-615-3559 www.plantsupport.com

Steam Trap Database Software Developer: Plant Support and Evaluations, Inc. Description: This free software was developed in Microsoft Access and is an open environment to enable anyone to make changes to meet their plant requirements.



### Spirax Sarco Application Engineering Department 1150 Northpoint Boulevard Blythewood, SC 29016 803-714-2000 www.spirax-sarco.com

SNAP3 Steam Needs Analysis Program Developer: Spirax Sarco Description: Total Steam System Software Programfor sizing and selecting: piping for steam/condensate/water, steam conditioning stations, pressure reducing stations, temperature control stations, steam traps (all types and applications), condensate recovery stations; flash steam recovery systems, clean/pure steam systems.

STMS Steam Trap Management System Developer: Spirax Sarco Description: Windows-based software designed for the easy collection, storage, organization, and sorting of steam trap data. It lets you createcustom databases from survey sheets or a handheld Data Collector, then analyze by maintenance schedules, trap performance, trap application or cost of steam loss, etc.



### Steam Conservation Systems 300 Summit Drive Cranston, RI 02920 401-944-2041 www.trapo.com

Steam $$ and the Trapo Demo Developer: Steam Conservation Systems Description: Calculates annual steam distribution system costs and efficiency demonstrates costs of energy lost through piping insulation, differentcosts of managing steam traps, shows investment, costs, payback and ROIs for changing to predictive maintenance. 

### Where to Find HelpA Sourcebook for Industry 

### 47 Where to Find Help

Thermon Corporation P.O. Box 609 San Marcus, TX 78667 800-820-4328 www.thermon.com



### SteamTrace 1.3 Developer: Thermon Corporation Description: Steam heat tracing design software.



### TLV Company, Ltd. 13901 South Lakes Drive Charlotte, NC 28273-6790 704-597-9070 www.tlv.com

TLV SE-1 STEAM Software Developer: TLV Company, Ltd. Description: Software to perform calculations for steam system components. Modules include Engineering Calculations, Steam Trap Selection,Pressure Reducing Valve Selection, Air Trap Selection, Gas Trap Selection, Air Vent Selection, Power Trap Selection, and Separator Selection.



### UE Systems 14 Hayes Street Elmsford, NY 10523 800-223-1325 www.uesystems.com

Ultraprobe 9000 Developer: UE Systems Description: Ultrasonic inspection and information storage system.



### U.S. Army Construction Engineering Laboratory P.O. Box 9005 Champaign, IL 61826 800-USA-CERL www.cecer.army.mil

HEATER Software Description: A computer modeling tool that incorporates the HEATMAP software. HEATER allows steam/condensate/utility systems to be modeled, and provides inventory and O&M condition indices that can be used to prioritize repairs/ replacement. Predictive modeling can estimate time to failure. 

### U.S. Department of Energy Industrial Technologies Program Room 5-F-065, MS EE-2F 1000 Independence Avenue, SW Washington, DC 20525 877-337-3463 www.eere.energy.gov/industry

3E Plus Insulation Appraisal software Developer: North American Insulation Manufacturers Association Description: Calculates insulation thickness to determine economic, energy, and environmental savings for piping and equipment. Includes calculations for heat gain or heat loss, surface temperature requirements, condensation control, heat loss efficiencies versus bare pipe, payback periods, and emissions reductions.



### Veritech Corporation 22960 Shaw Road, Suite 620 Sterling, VA 20166 703-435-78810 www.veritech-energy.com

ESteam Developer: Veritech Corporation Description: A steam system simulation program developed in a Microsoft Excel environment. The model performs heat and mass balances and allows flexibility for specifying c ondensate return, flash steam blowdown and deaeration schemes, letdown arrangements, and desuperheating configurations.



### Washington State University Cooperative Extension Energy Program 925 Plum Street, SE, Building 4 Olympia, WA 98504-3165 800-373-2139 www.wsu.edu

HEATMAP Software Description: HEATMAP is a software program that was specifically developed to help plan, analyze, and operate district heating and cooling systems.



### Yarway Corporation/Tyco Valve & Controls 9700 West Gulf Bank Road Houston, TX 72040 713-466-1176 www.yarway.comTrapMaster Developer: Yarway Corporation Description: Windows-based software designed for the collection, storage, organization, and sortingof steam trap data. It lets you create custom databases from survey sheets or a handheld Data Collector, then analyzes it in many different ways. It is possible to create a historical record of an individual trap’s performance over many surveys. An extensive database of steam trap manufacturer’s models and performance data is built in for easy access.

ASHRAE Journal American Society of Heating, Refrigeration, and Air Conditioning Engineers 1791 Tullie Circle, NE Atlanta, GA 30329 404-636-8400 www.ashrae.org

Boiler Systems Engineering American Boiler Manufacturers Association 1300 East 9th Street Cleveland, OH 44114 216-696-7000 www.hpac.com/BSE/

Chemical Engineering Chemical Week Publishing 110 William Street New York, NY 10138 212-621-4900 www.che.com

Chemical Processing Putman Media 555 West Pierce Road, Suite 301 Itasca, IL 60143 630-467-1300 www.chemicalprocessing.com

Consulting-Specifying Engineer Reed Business Information 360 Park Avenue South New York, NY 10014 646-746-6400 www.cahners.com

Energy Engineering Association of Energy Engineers 4025 Pleasantdale Road, Suite 420 Atlanta, GA 30340 770-447-5083 www.aeecenter.com

Energy User News Business News Publishing 1428-30 Midland Avenue #8 Bronxville, NY 10708 914-776-9241 www.energyusernews.com

Heating/Piping/Air Conditioning, HPAC, Engineering Penton Publishing 1300 East 9th Street Cleveland, OH 44114 216-696-7000 www.penton.com

Industrial Maintenance & Plant Operation (IMPO) Reed Business Information 360 Park Avenue South New York, NY 10014 646-746-6400 www.cahners.com

Mechanical Engineering, American Society of Mechanical Engineers (ASME) ASME International Three Park Avenue New York, NY 10016-5990 973-882-1167 www.asme.org

Plant Engineering Reed Business Information 360 Park Avenue South New York, NY 10014 646-746-6400 www.cahners.com

Plant Services Putnam Media 555 West Pierce, Suite 301 Itasca, IL 60143 630-467-1300 www.plantservices.com

Process Heating Business News Publishing Manor Oak One 1910 Cochran Road, Suite 450 Pittsburgh, PA 15220 412-531-3370 www.process-heating.com



### 48 Where to Find Help



## Periodicals

### American Gas Association (AGA) 400 North Capitol Street, NW Washington, DC 20001 202-824-7000 www.aga.org

Energy Analysis Description: Contains information on boilers in leading manufacturing industries as it relates to natural gas.

Solving Boiler Efficiency Problems Publication: Gas Technology: Natural Gas Applications in Industry, Summer 1996.



### Armstrong International, Inc. 816 Maple Street Three Rivers, MI 49093 269-273-1415 www.armintl.com

Capturing Energy Savings with Steam Traps Authors: Richard G. Bockwinkel and Scott A. French



### GTI 1700 South Mount Prospect Road Des Plaines, IL 60018 847-768-0500 www.gastechnology.org

Analysis of the Industrial Boiler Population Description: Report that identifies and characterizes the current industrial boiler population by fuel type and consumption, geographic location, industry, end user, and age. Publication, June 1993.



### United Kingdom Energy Efficiency Action Energy Web site Good Practice Guides +44 (0)08 0058 5794 www.actionenergy.co.uk

The Economic Thickness of Insulation for Hot Pipes Program: Available in: Fuel Efficiency Booklet 8 1994.

Improving Boiler Efficiency through Water Treatment Publication: Good Practice Guide 221, March 1998.

Reducing Energy Consumption Costs by Steam Metering Publication: Good Practice Guide 18, 1991. 

### U.S. Department of Energy Information Bridge P.O. Box 62 Oak Ridge, TN 37831 888-293-6498 www.osti.gov/bridge

Review of Orifice Plate Steam Traps Description: This report describes orifice traps andmechanical steam traps. It also provides information to help make decisions regarding applications for which orifice traps should be considered.



### U.S. Department of Energy Industrial Technologies Program Room 5-F-065, MS EE-2F 1000 Independence Avenue, SW Washington, DC 20525 877-337-3463 www.eere.energy.gov/industry

Overview of Energy Flow for Industries in Standard Industrial Classifications 20-39 Description: This report, sponsored by the Department of Energy’s Industries of the Future BestPractices activities, identifies and quantifies the energy supply and consumption in U.S. industry for heat and power by application.

Industrial Insulation for Systems Operating Above Ambient Temperature Description: This bulletin provides information about the use of thermal insulation on piping and flat surfaces where their temperatures are above that of their surroundings (ORNL/M-4678, 1995).

Steam Digest Description: This annual compendium is jointly published by the U.S. Department of Energy and the Alliance to Save Energy. It contains articles authored by a variety of manufacturers, national laboratories, and solution vendors. It covers the technical and managerial aspects of industrial steam facility optimization.



### AESYS Technologies 693 North Hills Road York, PA 17402-2212 717-755-1081 www.aesystech.com

Area(s) covered: AESYS Technologies offers courses 

## Training Courses and Technical Services Reports and Technical Papers

A Sourcebook for Industry 

### 49 Where to Find HelpImproving Steam System Performance in both boiler operation and maintenance, and facility operations and maintenance.



### American Boiler Manufacturers Association (ABMA) 4001 North 9th Street, Suite 226 Arlington, VA 22203-1900 703-522-7350 www.abma.com

ABMA members offer an extensive listing of training courses in many aspects of boiler operations and maintenance. Visit www.abma.com/training.php for details.



### American Society of Mechanical Engineers (ASME) Three Park Avenue New York, NY 10016-5990 800-843-2763 www.asme.org
Area(s) covered: The ASME gives courses on repairs and alterations of boilers and pressure vessels.



### Armstrong International, Inc. 816 Maple Street Three Rivers, MI 49093 269-273-1415 www.armintl.com

Area(s) covered: Armstrong International has trainingfacilities in which it sponsors Steam Energy Seminars and Education, and online steam training through Armstrong Steam University.



### Association of Energy Engineers (AEE) 4025 Pleasantdale Road, Suite 420 Atlanta, GA 30340 770-447-5083 www.aeecenter.org

Area(s) covered: • Industrial Energy Conservation • Strategies that Work • Optimizing Boiler Performance



### Babcock and Wilcox 20 South Van Buren Avenue Barberton, OH 44203-0351 330-753-4511 www.babcock.com

Area(s) covered: Babcock & Wilcox provide courses in: • Boiler Condition Assessment and Monitoring • Boiler Performance Analysis • Industrial Water-Tube Boiler • Oil/Gas-Fired Boilers



### Boiler Efficiency Institute P.O. Box 2255 Auburn, AL 36831-2255 800-669-6948 www.boilerinstitute.com

Area(s) covered: • Steam Plant Improvement • Workshop Engineering Fundamentals



### CDT Micrographics 137 Water Street Exeter, NH 03833 603-778-6140 www.cdtmicrographics.com

Area(s) covered: Hazards of Steam



### Center for Professional Advancement (CFPA) P.O. Box 7077 44 West Ferris Street East Brunswick, NJ 08816-7077 732-238-1600 www.cfpa.com

Area(s) covered: The CFPA offers courses in: • Boiler and Steam System Management • Boiler Water Treatment • Piping Design, Analysis, and Fabrication • Pressure Vessel Design and Analysis • Project Management for Plant Retrofits &

Shutdowns • Shell-and-Tube Heat Exchangers • Steam Turbines and Auxiliaries



### Eclipse Combustion, Inc. 1665 Elmwood Road Rockford, IL 61103 815-877-3031 www.eclipsenet.com

Area(s) covered: The Eclipse Combustion workshop is an accelerated three-day course covering the theory, design, operation, and application of industrial combustion equipment. • Combustion Fundamentals • Combustion Equipment



### 50 Where to Find Help

### 51 • Applications • Problem-solving and Troubleshooting • Plant Tour and Lab Demonstrations



### Enercheck Systems, Inc. P.O. Box 49426 Charlotte, NC 28277 704-841-9550 www.enerchecksystems.com

Area(s) covered: • Performing a Steam Trap Survey • Performing a Compressed Air/Inert Gas Survey • How to Make a Steam System Efficient



### Industrial Interactions, Inc./BEI 8302 Professional Hill Drive Fairfax, VA 22031 703-573-4500 www.wetrainindustry.com

Area(s) covered: Training courses in: • Boiler Operations and Maintenance • Industrial HVAC and Chillers • Facility Security and Emergency Guidelines • Water Chemistry in Boilers • Steam System Management

Technical and consulting services include: • Walk-through energy audits



### Johnson Controls Institute 5757 North Green Bay Avenue Milwaukee, WI 53201 414-524-1200 www.johnsoncontrols.com

Area(s) covered: • Heat Pump Controls • Boiler Maintenance • Specifying Facility Management Systems



### National Insulation Association (NIA) 99 Canal Center Plaza, Suite 222 Alexandria, VA 22314 703-683-6422 www.insulation.org

Area(s) covered: • Designing, specifying, and installing insulation • Accredited certification training in conducting

insulation energy appraisals 

### New York State Energy Research and Development Authority (NYSERDA) 17 Columbia Circle Albany, NY 12203-6399 518-862-1090 www.nyserda.org

Area(s) covered: NYSERDA offers a variety of opportunities for the commercial and industrial sectors in New York State to become more energy efficient. For current opportunities, visit www.nyserda.org



### North American Manufacturing Company 4455 East 71st Street Cleveland, OH 44105 216-271-6000 www.namfg.com

Area(s) covered: • Combustion and Kiln Control • Effective Combustion and Its Control • Optimizing Gas-Fired Industrial Heating

Processes 

### North Carolina State University Center for Boiler Studies Industrial Extension Services Campus Box 7902 Raleigh, NC 27695-7902 919-515-5438 www.ies.ncsu.edu

Area(s) covered: • Energy Management Techniques • Customized On-Site Boiler Seminars • Measuring and Improving Boiler Efficiency • An Evaluation of Oil vs. Natural Gas Firing

in Boilers • Improving Boiler Efficiency Through the Use

of Natural Gas



### PGS Energy Training Carnegie Office Park 600 North Bell Avenue Building 2, Suite 2708 Carnegie, PA 15106 412-279-9298 www.pgsenergy.com
Area(s) covered: Managing Industrial Energy Procurement

A Sourcebook for Industry 

### Where to Find Help

### 52 Plant Support & Evaluations, Inc. 282 Shellstone Court Naples, FL 34119 888-615-3559 www.plantsupport.com

Area(s) covered: • Steam System Training to Four Different Levels • Customized On-Site Boiler Training • Customized On-Site Complete Steam System

Training • Steam Trap Examiner Training (two levels) • Utility Optimization Training (steam and

compressed air) • Steam Start-up and Shut-down Procedure

Training • Defining and Resolving Waterhammer Training • On-site Steam System Assessments



### Power Specialties Company Inc. & Power Specialties Service P.O. Box 9566 Raytown, MO 64133 816-353-1740 www.powerspecialties.com

Area(s) covered: Power Specialties Company Inc. offers seminars to help optimize steam systems.



### Spirax Sarco Application Engineering Department 1150 Northpoint Boulevard Blythewood, SC 29016 803-714-2000 www.spirax-sarco.com

Area(s) covered: Spirax Sarco offers an open university program on clean steam utilization and a continuing education program on steam systems.



### Steam Conservation Systems 300 Summit Drive Cranston, RI 02920 401-944-2041 www.trapo.com

Area(s) covered: Steam Conservation Systems offers programs for reducing the costs and hassles of maintaining a steam distribution system. 

### Steam Economies Company 9325 Sutton Place Hamilton, OH 45011 513-874-8444 www.steameconomies.com

Area(s) covered: • Boiler & Steam System Fundamentals • Understanding Your Steam Boiler System



### University of Tennessee Energy, Environment and Resources Center 311 Conference Center Building Knoxville, TN 37996-4134 865-974-4251 eerc.ra.utk.edu

Area(s) covered: • Boiler & Steam System Fundamentals • Energy Management Techniques • Customized On-Site Boiler and Steam System

Seminars • Combined Heat and Power Fundamentals • Compressed Air Systems • On-site Assessments



### University of Wisconsin-Madison/Extension Department of Engineering Professional Development 432 North Lake Street Madison, WI 53706 800-462-0876 epdweb.engr.wisc.edu

Area(s) covered: The University of Wisconsin at Madison offers a course in Basic Boiler Water Treatment.



### Yarway Corporation/Tyco Valve & Controls 9700 West Gulf Bank Road Houston, TX 72040 713-466-1176 www.yarway.com
Area(s) covered: 1 or 2 1/2 day courses covering Steam Conservation, Steam and Condensate Systems, Steam Trapping, Installation and Maintenance.

Improving Steam System Performance 

### Where to Find HelpA Sourcebook for Industry 

### 53 Where to Find Help

Armstrong International, Inc. 816 Maple Street Three Rivers, MI 49093 269-273-1415 www.armintl.com

Guidelines for the Prevention of Water Hammer Description: Video identifies the most likely causes of water hammer and provides solutions that can be implemented to prevent it. (16 minutes)
Guidelines for Steam System Efficiency Description: Video explaining basic considerations in the design, piping, and trapping of steam systems. (15 minutes)

Guidelines for Steam Trap Troubleshooting and Testing Description: Video outlining the need for establishing a preventive maintenance program and details what to look and listen for in testing steam traps. (18 minutes)

Let's Talk Steam Traps/Update Description: Video explaining the operating principles of the three types of steam traps: mechanical, thermostatic, and thermodynamic. This tape helps users understand the internal operation of inverted bucket, F&T, thermostatic, and disc traps. (32 minutes)

What Is Steam? Description: Video explaining the basics of steam. (15 minutes)



### International District Energy Association 125 Turnpike Road, Suite 4 Westborough, MA 01581-2841 508-366-9339 www.districtenergy.org

Steam Distribution System Safety – A Video Training Program Description: The purpose of this video training program is to present the operating features of a typical District Heating System with special emphasis on hazards and safety procedures. 

### Spirax Sarco Application Engineering Department 1150 Northpoint Boulevard Blythewood, SC 29016 803-714-2000 www.spirax-sarco.com

Effective Condensate Drainage from Heat Exchangers Description: This video highlights the operation of steam process equipment during change in demand to address known problems of water hammer and temperature fluctuations. (15 minutes)

Steam Boilers: The Inside Information Description: The video highlights internal boiler response to on/off demand, high steam demand, reduced boiler pressure, and change in total dissolved solids (TDS). (12 1/2 minutes) 

## VideosImproving Steam System Performance 

### 54 Where to Find Help◆ 

### Appendix A: Glossary of Terms This appendix contains a glossary of terms used in steam systems.

◆ 

### Appendix B: Tip Sheets This appendix contains a series of steam system tip sheets. Developed by the U.S. Department of Energy, these tip sheets discuss common opportunities that industrial facilities can use to improve performance and reduce fuel use.

◆ 

### Appendix C: Guidelines for Comment This appendix contains a form that provides a vehicle for submitting comments for improving the Sourcebook. 

# Appendices

55 A Sourcebook for Industry 

### Appendices

The following appendices have been included in the Sourcebook:Improving Steam System Performance 

### 56 AppendicesA Sourcebook for Industry 

### 57 Absorption chilling—This is a water chillingprocess in which cooling of a solution is accomplished by the evaporation of a fluid (usually water), which is then absorbed by a differentsolution (usually lithium bromide), then evaporated under heat and pressure. The fluid is thencondensed with the heat of condensation rejected through a cooling tower.

Air vent—A device that allows the release of non-condensable gases from a steam system.

Alkalinity—A measure of the concentration of carbonate, bicarbonate, and hydroxyl ion in water, usually expressed in equivalent ppm (parts per million) of calcium carbonate.

Backpressure turbine—A turbine that exhausts steam above atmospheric pressure. The exhaust steam is usually sent to other services.

Biomass—Organic matter which is available on a renewable basis, including agricultural crops and agricultural wastes and residues, wood and wood wastes and residues, animal wastes, municipal wastes, and aquatic plants.

Blowdown ratio—For boilers, the ratio of waterremoved by blowdown to the amount of feedwater provided to the boiler in equivalent units for the same time period (both usually reported in pounds per hour).

Boiler—A vessel or tank in which heat produced from the combustion of fuels such as natural gas, fuel oil, wood, or coal is used to generate hot water or steam for applications ranging from building space heating to electric power production or industrial process heat.

Boiler blowdown—The periodic or continuous removal of water from a boiler to remove concentrations of dissolved solids and/or sludge accumulating in the boiler. Boiler horsepower—A unit of rate of water evaporation equal to the evaporation per hour of 34.5 pounds of water at a temperature of 212°F into steam at 212°F. One boiler horsepower equals 33,475 Btu per hour.

British thermal unit (Btu)—The amount of heat required to raise the temperature of one pound of water one degree Fahrenheit; equal to 252 calories. It is roughly equal to the heat of one kitchen match.

Chlorides—Chemical compounds found in boiler water consisting of metallic ions with chlorine atoms, part of a group of compounds called salts. The most prevalent are magnesium chloride and sodium chloride.

Cogeneration—The simultaneous production of electrical or mechanical work and thermal energy from a process, thus reducing the amount of heat or energy lost from the process. Also known as combined heat and power (CHP).

Combined Heat and Power (CHP)—The simultaneous production of electrical or mechanical work and thermal energy from a process, thus reducing any waste heat or energy lost from the process. Also known as cogeneration.

Combustion efficiency—This measure represents the amount of fuel energy extracted from flue gases. It is a steady state measure and doesnot include boiler shell losses or blowdown losses. The losses identified in this efficiency calculation are the stack losses. Stack loss is an indication of the amount of energy remaining in the flue gases as they exit the boiler.

Combustion turbine—A turbine that generates electric power from the combustion of a fuel.

Condensate—Condensed steam.

Condensate pump—A pump that pressurizescondensate allowing it to flow back to a collection tank, or boiler plant. 

### Appendix A: Glossary of Terms



# Appendix A: Glossary of TermsImproving Steam System Performance 

### 58 Condenser—A device that condenses steam. Surface condensers use a heat exchanger to remove energy from the steam, and typically operate under vacuum conditions.

Condensing turbine—A turbine that exhausts steam to typically sub-atmospheric conditions where the steam is condensed. These turbines are usually used in power generation applications.

Continuous blowdown— The process of removing water, on a continuous basis, from a boiler to remove high concentrations of dissolved solids, chlorides, and other products. Water is replaced by treated make-up water added to the condensate return. The withdrawn blowdown water is usually discharged to a sanitary drain.

Deaerator—A device that uses steam to strip feedwater of oxygen and carbon dioxide.

Desuperheater—A device used in steam systems to control the energy level and/or temperature ofsteam supplied to an end use, typically by injecting a fine mist of condensate into the steam flow.

Dew point—The temperature to which a vapor must be cooled, in order for saturation or condensation to occur.

Dissolved solids—The minerals and impurities in boiler make-up water. These increase in concentration as water is boiled into steam.

Distillation column—A device that separatescomponents of a compound relying on differences in boiling points.

Dryer—A device that removes moisture from a solid.

Duty cycle—The duration and periodicity of the operation of a device.

Excess air—Excess air in a combustion process is that amount of air present in excess of the theoretically required air for complete combustion.Excess air absorbs some of the heat of combustion and is carried away as waste heat with the exhaust combusted gases.

Evaporator—A device that removes moisturefrom a liquid, resulting in increased concentration of the remaining compounds. Feedwater—Water sent into a boiler or a steam generator. Feedwater typically meets cleanliness criteria, contains treatment chemicals, and has been stripped of oxygen.

Feedwater pump—A pump that sufficiently pressurizes feedwater to supply a boiler or generator.

Full load efficiency—The stated efficiency (in percent) of a process in terms of energy or work output divided by energy input at rated production (full load).

Greenhouse gas emissions—Those gases, such as water vapor, carbon dioxide, tropospheric ozone,methane, and low level ozone that are transparent to solar radiation, but opaque to long wave radiation, and which are believed to contribute to climate change.

Heat exchanger—A device used to transfer heat from one medium by either direct or indirect contact.

Heating, Ventilating and Air Conditioning (HVAC)—All the components of the appliance or system used to condition the interior air of a facility.

Heat Recovery Steam Generator (HRSG)— A device that captures the thermal energy in an exhaust stream or a process stream and transfers it to water to generate steam.

Kilowatt hour (kWh)—A unit of measure of electricity supply or consumption of 1,000 Watts over the period of one hour; equivalent to 3,412 Btu.

Latent heat—The change in heat content that occurs with a change in phase and without change in temperature. Changes in heat content that affect a change in temperature are called sensible heat changes.

Life Cycle Cost (LCC)—The sum of all the costs both recurring and nonrecurring, related to a product, structure, system, or service during its life span or specified time period. 

### Appendix A: Glossary of TermsA Sourcebook for Industry 

### 59 Make-up water—Water brought into a boiler system from outside to replace condensate notreturned to the boiler plant, water used in blowdown, steam lost through leaks, or water lost through evaporation or mist.

MMBtu—A unit of one million British thermal units (Btu).

Payback—The amount of time required for positive cash flows to equal the total investment costs. This is often used to describe how long it will take for energy savings resulting from using more energy-efficient equipment to equal thepremium paid to purchase the more energy-efficient equipment.

Potable water—Water that is suitable for drinking, as defined by local health officials.

Pounds per square inch gauge (psig)— A unit of pressure in pounds force in comparison to local atmospheric pressure (as measured by a gauge).

Pressure Reducing Valve (PRV)—A valve that regulates the amount of steam allowed from a high-pressure service to a low-pressure service.

Radiant energy—Energy (transfer of heatthrough matter or space by means of electromagnetic waves) that transmits away from its source in all directions.

Reboiler—A heat exchanger used in petroleumrefining and chemical manufacturing applications that adds heat to a process stream.

Reformer—A device that produces hydrogen from a hydrocarbon compound such as methane, typically by using steam.

Relative humidity—A measure of the percent of moisture actually in the air compared with what would be in it if it were fully saturated at that temperature. When the air is fully saturated, its relative humidity is 100 percent.

R-Value—A measure of the capacity of a material (or assembly of materials) to resist heat transfer, sometimes called thermal resistance. The R-Value is the reciprocal of the heat transfer coefficient (U-Value). The larger the R-Value, the greater its insulating properties. Silica—The concentration of silica dioxide found in water measured in parts per million. Silicaforms a tenacious scale with low thermal conductance. Silica is soluble in steam and can carryover into steam where it can condense on turbine blades or erode surfaces.

Sludge—A general term applied to a relatively loose accumulation of material that has settled to the bottom of a boiler.

Stack heat loss—Sensible and latent heat contained in combustion gases and vapor emitted to the atmosphere.

Stand-alone—A device that operates independent of or is not connected to other systems.

Standby losses—In boiler systems, standby losses are energy losses that are associated with natural draft through a boiler in a standby operating mode.

Steam ejector—A device that uses a relativelyhigh-pressure motive steam flow through a nozzle to create a low-pressure or suction effect.

Steam injector—A device that injects steam into a process, often used in direct steam heating applications.

Steam trap—An automatic control valve that allows for the release of condensate, air, CO 2, and other non-condensable gases, yet keeps live steam in the system.

Stripper—A device that separates components from a compound.

Surface blowdown—Boiler blowdown taken from the upper part of the boiler just below the water surface to reduce the amount of dissolved solids.

Thermal conductivity—This is a positive constant, k, that is a property of a substance and is used in the calculation of heat transfer rates for materials. It is the amount of heat that flowsthrough a specified area and thickness of a material over a specified period of time when there is a temperature difference of one degree between the surfaces of the material. 

### Appendix A: Glossary of TermsImproving Steam System Performance 

### 60 Thermal load factor—A term used to describe the relative stability of use of heating in a facility or a process. Often used in cogeneration where a “high” factor denotes a continuous use of steady heating.

Thermocompressor—A device that uses highpressure steam to increase the pressure of a lowpressure steam supply to generate a more useful steam service.

Throttling—Regulating flow rate by closing a valve in the system.

Turbine—A device that converts the enthalpy of steam into mechanical work. See condensing turbine and backpressure turbine.

Vacuum breaker—A device that responds to the formation of vacuum conditions in equipment such as a heat exchanger by allowing in air which promotes condensate drainage.

Variable Frequency Drive (VFD)—A type of variable speed motor drive in which the motor is supplied with electrical power at frequencies other than standard 60 Hertz through a converter.

Variable Air Volume (VAV)—Variable air volume is a term for changing the quantity of air flow to meet heating, cooling, or exhaust loads rather than changing air temperatures.

Waste heat—Heat that is discharged from a mechanical process, wastewater, or ventilation exhaust system that could be reclaimed for useful purposes.

Water hammer—A shock that results from the sudden collapse of a steam pocket in a two phase line such as a condensate return line. Also the impingement of a water slug carried by relatively high velocity steam.



### Appendix A: Glossary of TermsA Sourcebook for Industry 

### 61 Appendix B: Steam Tip Sheets



# Appendix B: Steam Tip Sheets

Some improvement opportunities are available to many different systems. To increase industry awareness of several fundamental improvement opportunities, the U.S. Department of Energy’s Industrial Technologies Program has developed the following tip sheets through its BestPractices activities.

1. Inspect and Repair Steam Traps
2. Insulate Steam Distribution and Condensate Return Lines 3. Use Feedwater Economizers for Waste Heat Recovery 4. Improve Your Boiler's Combustion Efficiency 5. Tip Sheet Number Skipped 6. Tip Sheet Number Skipped
7. Clean Boiler Waterside Heat Transfer Surfaces
8. Return Condensate to the Boiler
9. Minimize Boiler Blowdown
10. Recover Heat from Boiler Blowdown 11. Use Vapor Recompression to Recover Low-Pressure Waste Steam 12. Flash High-Pressure Condensate to Regenerate Low-Pressure Steam 13. Use a Vent Condenser to Recover Flash Steam Energy 14. Use Low-Grade Waste Steam to Power Absorption Chillers
15. Benchmark the Fuel Costs of Steam Generation 16. Minimize Boiler Short Cycling Losses 17. Install Removable Insulation on Valves and Fittings 18. Deaerators in Industrial Steam Systems 19. Cover Heated, Open Vessels 20. Replace Pressure-Reducing Valves with Backpressure Turbogenerators 21. Consider Steam Turbine Drives for Rotating Equipment 22. Consider Installing High-Pressure Boilers with Backpressure Turbine-Generators 23. Install an Automatic Blowdown Control System 24. Upgrade Boilers with Energy-Efficient Burners 25. Consider Installing Turbulators on Two- and Three-Pass Firetube BoilersImproving Steam System Performance 

### 62 Appendix B: Steam Tip Sheets

# Inspect and Repair Steam Traps

In steam systems that have not been maintained for three to five years, between 15% to 30% of the installed steam traps may have failed—thus allowing live steam to escape into the condensate return system. In systems with a regularly scheduled maintenance program, leaking traps should account for less than 5% of the trap population. If your steam distribution system includes more than 500 traps, a steam trap survey will probably reveal significant steam losses.

◆ 

### Example In a plant where the value of steam is $4.50 per thousand pounds ($/1,000 lbs), an inspection program indicates that a trap on a 150 psig steam line is stuck open. The trap orifice is 1/8 inch in diameter. The table shows the estimated steam loss as 75.8 lbs/hr. By repairing the failed trap, annual savings are:

Savings = 75.8 lbs/hr x 8,760 hrs/yr x $4.50/1,000 lbs = $2,988/yr

◆ 

### Steam Trap Testing Facts Steam traps are tested to determine if they are functioning properly and not cold plugging or failing in an open position and allowing live steam to escape intothe condensate return system. There are four basic ways to test steam traps: temperature, sound, visual, and electronic.

A Sourcebook for Industry 

### 63 Appendix B: Steam Tip Sheet Number 1

Recommended Steam Trap Testing Intervals • High Pressure (150 psig and

above): Weekly to Monthly • Medium Pressure (30 to 150

psig): Monthly to Quarterly • Low Pressure (Below 30 psig):

Annually

◆ 

### Suggested Actions ◆ Steam traps are tested primarily to determine whether they are functioning properly and not allowing live steam to blow through . Establish a program for the regular systematic inspection, testing, and repair of steam traps. Include a reporting mechanism to ensure thorou ghness and to provide a means of documenting energy and dollar savings.

Steam Tip Sheet information is adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102002-1503 • March 2002 • Steam Tip Sheet #1 Steam Loss (lbs/hr) Trap Orifice Steam Pressure (psig) Diameter (inches) 15 100 150 300
1/32 0.85 3.3 4.8 –
1/16 3.4 13.2 18.9 36.2
1/8 13.7 52.8 75.8 145
3/16 30.7 119 170 326
1/4 54.7 211 303 579
3/8 123 475 682 1,303 From the Boiler Efficiency Institute. Steam is discharging to atmospheric pressure.

Leaking Steam Trap Discharge Rate

# Insulate Steam Distribution and Condensate Return Lines

Uninsulated steam distribution and condensate return lines are a constant sourceof wasted energy. The table shows typical heat loss from uninsulated steam distribution lines. Insulation can typically reduce energy losses by 90% and help ensure proper steam pressure at plant equipment. Any surface over 120°F should be insulated, including boiler surfaces, steam and condensate return piping, and fittings.

Insulation frequently becomes damaged or is removed and never replaced duringsteam system repair. Damaged or wet insulation should be repaired or immediately replaced to avoid compromising the insulating value. Eliminate sources ofmoisture prior to insulation replacement. Causes of wet insulation include leaking valves, external pipe leaks, tube leaks, or leaks from adjacent equipment. After steam lines are insulated, changes in heat flows can influence other parts of the steam system.



### ◆ Example In a plant where the value of steam is $4.50/MMBtu, a survey of the steam system identified 1,120 feet of bare 1-inch diameter steam line, and 175 feet of bare 2-inch line both operating at 150 psig. An additional 250 feet of bare 4-inch diameter line operating at 15 psig was found. From the table, the quantity of heat lost per year is:

1-inch line: 1,120 feet x 285 MMBtu/yr per 100 ft = 3,192 MMBtu/yr 2-inch line: 175 feet x 480 MMBtu/yr per 100 ft = 840 MMBtu/yr 4-inch line: 250 feet x 415 MMBtu/yr per 100 ft = 1,037 MMBtu/yr Total Heat Loss = 5,069 MMBtu/yr The annual operating cost savings from installing 90% efficient insulation is: 0.90 x $4.50/MMBtu x 5,069 MMBtu/yr = $20,530 Heat Loss per 100 feet of Uninsulated Steam Line (MMBtu/yr)
Distribution Line Steam Pressure (psig) Diameter (inches) 15 150 300 600
1 140 285 375 495
2 235 480 630 840 4 415 850 1,120 1,500 8 740 1,540 2,030 2,725 12 1,055 2,200 2,910 3,920 Based on horizontal steel pipe, 75oF ambient air, no wind velocity, and 8,760 operating hr/yr.

Improving Steam System Performance 

### 64 Appendix B: Steam Tip Sheet Number 2

Insulation Optimization Software Available

The North American Insulation Manu-facturers Association has developed a software package (3EPlus) that determines the optimum thickness for a wide variety of insulating materials. Outputs include the simple payback period, surface heat loss, and surface temperature for each specified insulation thickness. 3EPlus is available at no cost through the EERE Information Center, 877-337-3463.



### Use Insulating Jackets Removable insulating jackets are available for valves, flanges, steam traps, and other fittings. Remember that a 6-inch gate valve may have over 6 square feet of surface area from which to radiate heat.

◆ 

### Suggested Actions ◆ Conduct a survey of your steam distribution and condensate return piping, install insulation, and start to save.

Steam Tip Sheet information is adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102002-1504 • March 2002 • Steam Tip Sheet #2 Heat Loss per 100 feet of Uninsulated Steam Line

# Use Feedwater Economizers for Waste Heat Recovery

A feedwater economizer reduces steam boiler fuel requirements by transferring heat from the flue gas to incoming feedwater. Boiler flue gases are often rejectedto the stack at temperatures more than 100°F to 150°F higher than the temperature of the generated steam. Generally, boiler efficiency can be increased by 1% for every 40°F reduction in flue gas temperature. By recovering waste heat, an economizer can often reduce fuel requirements by 5% to 10% and pay for itself in less than 2 years. The table provides examples of the potential for heat recovery.

◆ 

### ExampleA boiler generates 45,000 lb/hr of 150 psig steam by burning natural gas. Condensate is returned to the boiler and mixed with makeup water to yield 117°F feedwater. The stack temperature is measured at 500°F. Determine the annual energy savings that will be achieved by installing an economizer given 8,400 hours per year of boiler operation at an energy cost of $4.50/MMBtu. From the steam tables, the following enthalpy values are available:

For 150 psig saturated steam: 1,195.50 Btu/lb For 117°F feedwater: 84.97 Btu/lb Boiler thermal output = 45,000 lb/hr x (1,195.5 – 84.97) Btu/lb = 50 million Btu/hr The recoverable heat corresponding to a stack temperature of 500°F and a natural gas-fired boiler load of 50 MMBtu/hr is read from the table (above) as 4.6 MMBtu/hr. Annual savings = 4.6 MMBtu/hr x $4.50/MMBtu x 8,400 hr/yr = $173,880/yr 

### Exhaust Gas Temperature Limits The lowest temperature to which flue gases can be cooled depends on the type of fuel used: 250°F for natural gas, 300°F for coal and low sulphur content fuel oils, and 350°F for high sulphur fuel oils. These limits are set to prevent condensation and possible corrosion of the stack.



### Potential Economizer Applications
A feedwater economizer is appropriate when insufficient heat transfer surface exists within the boiler to remove combustion heat. Boilers that exceed 100 boiler hp, operating at pressures exceeding 75 psig or above, and that are significantly loaded all year long are excellent candidates for an economizer retrofit.

◆ 

### Suggested Actions ◆ • Determine the stack temperature after the boiler has been tuned to manufacturer’s specifications. The boiler should be operati ng at

close-to-optimum excess air levels with all heat transfer surfaces clean. • Determine the minimum temperature to which stack gases can be cooled subject to criteria such as dew point, cold-end corrosion,

and economic heat transfer surface. (See sidebar: Exhaust Gas Temperature Limits.) • Study the cost-effectiveness of installing a feedwater economizer or air preheater in your boiler. Recoverable Heat, MMBtu/hr
Initial Stack Gas Boiler Thermal Output, MMBtu/hr Temperature, °F 25 50 100 200
400 1.3 2.6 5.3 10.6
500 2.3 4.6 9.2 18.4
600 3.3 6.5 13.0 26.1
Based on natural gas fuel, 15% excess air, and a final stack temperature of 250°F.

A Sourcebook for Industry 

### 65 Steam Tip Sheet information is adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102002-1505 • March 2002 • Steam Tip Sheet #3 

### Appendix B: Steam Tip Sheet Number 3

Recoverable Heat from Boiler Flue Gases

# Improve Your Boiler’s Combustion Efficiency

Combustion Efficiency Operating your boiler with an optimum amount of excess air will minimize heat loss up the stack and improve combustion efficiency. Combustion efficiency is a measure of how effectively the heat content of a fuel is transferred into usableheat. The stack temperature and flue gas oxygen (or carbon dioxide) concentrations are primary indicators of combustion efficiency. Given complete mixing, a precise or stoichiometric amount of air is required to completely react with a given quantity of fuel. In practice, combustion conditions are never ideal, and additional or “excess” air must be supplied to completely burn the fuel. The correct amount of excess air is determined from analyzing flue gas oxygen or carbon dioxide concentrations. Inadequate excess air results in unburned combustibles (fuel, soot, smoke, and carbon monoxide) while too much results in heat lost due to the increased flue gas flow—thus lowering the overall boiler fuel-to-steam efficiency. The table relates stack readings to boiler performance.

On well-designed natural gas-fired systems, an excess air level of 10% is attainable. An often stated rule of thumb is that boiler efficiency can be increased by 1% for each 15% reduction in excess air or 40°F reduction in stack gas temperature.

◆ 

### Example A boiler operates for 8,000 hours per year and consumes 500,000 MMBtu of natural gas while producing 45,000 lb/hr of 150 psig steam. Stack gas measurementsindicate an excess air level of 44.9% with a flue gas less combustion air temperature of 400°F. From the table, the boiler combustion efficiency is 78.2% (E1). Tuning the boiler reduces the excess air to 9.5% with a flue gas less combustion air temperature of 300°F. The boiler combustion efficiency increases to 83.1% (E2). Assuming a steam value of $4.50/MMBtu, the annual cost savings are:

Cost Savings = Fuel Consumption x (1 - E1/E2) x steam cost = 29,482 MMBtu/yr x $4.50/MMBtu = $132,671 annually Combustion Efficiency
Excess % Flue Gas Temperature Less Combustion Air Temp, °F Air Oxygen 200 300 400 500 600
9.5 2.0 85.4 83.1 80.8 78.4 76.0
15.0 3.0 85.2 82.8 80.4 77.9 75.4
28.1 5.0 84.7 82.1 79.5 76.7 74.0
44.9 7.0 84.1 81.2 78.2 75.2 72.1
81.6 10.0 82.8 79.3 75.6 71.9 68.2



### 66 Improving Steam System Performance 

### Flue Gas Analyzers The percentage of oxygen in the flue gas can be measured by inexpensive gas-absorbing test kits. More expensive ($500-$1,000) hand-held, computer-based analyzers display percent oxygen, stack gas temperature, and boilerefficiency. They are a recommended investment for any boiler system with annual fuel costs exceeding $50,000.



### Oxygen Trim Systems When fuel composition ishighly variable (such as refinery gas, hog fuel, or multi-fuel boilers), or where steam flows are highly variable, an on-line oxygen analyzer should be considered. The oxygen “trim” system provides feedback tothe burner controls to automatically minimize excess combustion air and optimize the air-to-fuel ratio.

Assumes complete combustion with no water vapor in the combustion air.

Steam Tip Sheet information is adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102002-1506 • March 2002 • Steam Tip Sheet #4 ◆ 

### Suggested Actions ◆ Boilers often operate at excess air levels higher than the optimum. Periodically monitor flue gas composition and tune your boi lers to maintain excess air at optimum levels. 

### Appendix B: Steam Tip Sheet Number 4

Combustion Efficiency for Natural Gas

# Clean Boiler Waterside Heat Transfer Surfaces

Even on small boilers, the prevention of scale formation can produce substantialenergy savings. Scale deposits occur when calcium, magnesium, and silica, commonly found in most water supplies, react to form a continuous layer of material on the waterside of the boiler heat exchange tubes. Scale creates a problem because it typically possesses a thermal conductivity an order of magnitude less than the corresponding value for bare steel. Even thin layers of scale serve as an effective insulator and retard heat transfer. The result is overheating of boiler tube metal, tube failures, and loss of energy efficiency. Fuelwaste due to boiler scale may be 2% for water-tube boilers and up to 5% in firetube boilers. Energy losses as a function of scale thickness and composition are given in the table below.

◆ 

### Example A boiler annually uses 450,000 million Btu (MMBtu) of fuel while operating for 8,000 hours at its rated capacity of 45,000 pounds-per-hour (lbs/hr) of 150-psig steam. If scale 1/32nd of an inch thick is allowed to form on the boiler tubes, and the scale is of “normal” composition, the table indicates a fuel loss of 2%. The increase in operating costs, assuming energy is priced at $3.00/MMBtu, is: Annual Operating Cost Increase = 450,000 MMBtu/year x $3.00/MMBtu x 0.02

= $27,000 Fuel Loss, % of Total Use Scale Thickness, Scale Type inches “Normal” High Iron Iron Plus Silica
1/64 1.0 1.6 3.5
1/32 2.0 3.1 7.0
3/64 3.0 4.7 –
1/16 3.9 6.2 –



### 67 A Sourcebook for Industry 

### Monitor Flue Gas Temperature
An indirect indicator of scale or deposit formation is flue gas temperature. If the flue gas temperature rises (with boilerload and excess air held constant), the effect is possibly due to the presence of scale.



### Perform Visual Inspections Visually inspect boiler tubes when the unit is shut down for maintenance. Scale removal can be achieved by mechanical means or acid cleaning. If scale is present, consult with your local water treatment specialist and consider modifying your feedwater treatment or chemical additives schedule.

◆ 

### Suggested Actions ◆ Any scale in a boiler is undesirable. The best way to deal with scale is not to let it form in the first place. Scale formationis prevented by: • Pretreatment of boiler make-up water (using water softeners, demineralizers, and reverse osmosis to

remove scale-forming minerals), • Chemical injection into the boiler feedwater, and • Adopting proper boiler blowdown practices. Note: “Normal” scale is usually encountered in low-pressure applications. The high iron and iron plus silica scale composition results from high-pressure service conditions. *Extracted from National Institute of Standards and Technology, Handbook 115, Supplement 1.

Steam Tip Sheet information is adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-10099-952 • Revised June 2001 • Steam Tip Sheet #7 Energy Loss Due to Scale Deposits* 

### Appendix B: Steam Tip Sheet Number 7

# Return Condensate to the Boiler

When steam transfers its heat in a manufacturing process, heat exchanger, or heating coil, it reverts to a liquid phase called condensate. An attractive method of improving your power plant’s energy efficiency is to increase the condensate return to the boiler. Returning hot condensate to the boiler makes sense for several reasons. As more condensate is returned, less make-up water is required, saving fuel, make-up water, and chemicals and treatment costs. Less condensate discharged into a sewer system reduces disposal costs. Return of high purity condensate also reduces energy losses due to boiler blowdown. Significant fuel savings occur as most returned condensate is relatively hot (130°F to 225°F), reducing the amount of cold make-up water (50°F to 60°F) that must be heated. A simple calculation indicates that energy in the condensate can be more than 10% of the total steam energy content of a typical system. The graph shows the heat remaining in the condensate at various condensate temperatures, for a steam system operating at 100 psig, with make-up water at 55°F.

◆ 

### Example Consider a steam system that returns an additional 10,000 lbs/hr of condensate at 180°F due to distribution modifications. Assume this system operates 8,000 hours annually with an average boiler efficiency of 82%, and make-up water temperature of 55°F. The water and sewage costs for the plant are $0.002/gal, and the water treatment cost is $0.002/gal. The fuel cost is $3.00 per Million Btu (MMBtu). Assuming a 12% flash steam loss*, calculate the overall annual savings. Annual Water, Sewage, and Chemicals Savings = (1 – Flash Steam Fraction) x (Condensate Load in lbs/hr) x Annual Operating Hours x (Total Water Costs in $/gal) ÷ (Water Density in lbs/gal)

= (1 - 0.12) x 10,000 x 8,000 x $0.004 = $33,760 8.34
* When saturated condensate is reduced to some lower pressure, some condensate flashes off to steam again.

This amount is the flash steam loss. Annual Fuel Savings = (1 – Flash Steam Fraction) x (Condensate Load in lbs/hr) x Annual Operating Hours x (Makeup Water Temperature rise in °F) x (Fuel Cost in $/Btu) ) ÷ Boiler Efficiency

= (1 - 0.12) x 10,000 x 8,000 x (180 – 55) x $3.00 = $32,195 0.82 x 106 Total Annual Savings Due to Return of an Additional 10,000 lbs/hr of Condensate = $33,760 + $32,195 = $65,955



### 68 Improving Steam System Performance Steam Tip Sheet information is adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-10099-953 • Revised June 2001 • Steam Tip Sheet #8 

### Condensate Recovery Produces Savings A large specialty paper plant reduced its boiler makeup water rate from about 35% of steam production to between 14% and 20% by returning additional condensate. Annual savings added up to more than $300,000.



### Suggested Actions Reduce operating costs through maximizing the return of hotcondensate to the boiler. Consider the following actions: • If a condensate return system

is absent, estimate the cost of a condensate return andtreatment system (as necessary) and install one if economically justified. • Repair steam distribution

and condensate return system leaks.
• Insulate condensate return

system piping to conserve heat and protect personnel against burns. 12 5 17 5 225 275 325 25

20

15

10

5

0Heat Remainingin Condensate (%)

15 0 2 00 250 300 350 Condensate Temperature ( ° F) Let: h c = enthalpy of condensate at 180°F = 148 Btu/lb hm = enthalpy of make-up water at 55°F = 23 Btu/lb h s = enthalpy of steam at 100 psig = 1189 Btu/lb Heat remaining in condensate (%):
= (h c – hm)/(h s – hm) x 100
= (148 – 23)/(1189 – 23) x 100 = 10.7% 

### Appendix B: Steam Tip Sheet Number 8

### 69 A Sourcebook for Industry 

# Minimize Boiler Blowdown

Minimizing your blowdown rate can substantially reduce energy losses, as the temperature of the blown-down liquid is the same as that of the steam generated in the boiler. Minimizing blowdown will also reduce makeup water and chemical treatment costs. As water evaporates in the boiler steam drum, solids present in the feedwater are left behind. The suspended solids form sludge or sediments in the boiler, which degrades heat transfer. Dissolved solids promote foaming and carryover of boiler water into the steam. To reduce the levels of suspended and total dissolved solids (TDS) to acceptable limits, water is periodically discharged or blown down from the boiler. Mud or bottom blowdown is usually a manual procedure done for a few seconds on intervals of several hours. It is designed to remove suspended solids that settle out of the boiler water and form a heavy sludge. Surface or skimming blowdown is designed to remove the dissolved solids that concentrate near the liquid surface. Surface blowdown is often a continuous process. Insufficient blowdown may lead to carryover of boiler water into the steam, or the formation of deposits. Excessive blowdown will waste energy, water, andchemicals. The optimum blowdown rate is determined by various factors including the boiler type, operating pressure, water treatment, and quality of makeup water. Blowdown rates typically range from 4% to 8% of boiler feedwater flow rate, but can be as high as 10% when makeup water has a high solids content.

◆ 

### ExampleAssume that the installation of an automatic blowdown control system (see sidebar) reduces your blowdown rate from 8% to 6%. This example assumes a continuously operating natural-gas-fired, 150-psig, 100,000-pound-per-hour steam boiler. Assume a makeup water temperature of 60°F, boiler efficiency of 82%, with fuel valued at $3.00 per million Btu (MMBtu), and the total water, sewage and treatment costs at $0.004 per gallon. Calculate the total annual cost savings.

Boiler Feedwater: Initial = 100,000 = 108,695 lbs/hr (1 - 0.08)

Final = 100,000 = 106,383 lbs/hr (1 - 0.06)
Makeup Water Savings = 108,695 – 106,383 = 2312 lbs/hr Enthalpy of boiler water = 338.5 Btu/lb; for makeup water at 60°F = 28 Btu/lb Thermal Energy Savings = 338.5 – 28 = 310.5 Btu/lb

Annual Fuel Savings = 2312 lbs/hr x 8760 hrs/yr x 310.5 Btu/lb x $3.00/MMBtu = $23,007 0.82 x 10 6 Annual Water and Chemical Savings = 2312 lbs/hr x 8760 hrs/yr x$0.004/gal = $9,714 8.34 lbs/gal Annual Cost Savings = $23,007 + $9,714 = $32,721 

### Automatic Blowdown Control Systems These systems optimize surface blowdown by regulating water volume discharged in relation to amount of dissolved solids present. Conductivity, TDS,silica or chlorides concentrations, and/or alkalinity are reliable indicators of salts and other contaminants dissolvedin boiler water. A probe provides feedback to a controllerdriving a modulating blowdown valve. An alternative is proportional control —withblowdown rate set proportional to makeup water flow.



### Cycles of Concentration “Cycles of concentration” refers to the accumulation of impurities in the boiler water. If the boiler water containsten times the level of impurities in the makeup water, it is said to have ten cycles of concentration.

References and Footnotes

1. Consensus Operating Practices for

Control of Feedwater/Boiler Water Chemistry in Modern Industrial Boilers, published by the ASME, 1994.

2. Recommended Rules for the Care and

Operation of Heating Boilers , Section VI of the ASME Boiler and Pressure Vessel Code, 1995.

3. Recommended Guidelines for the Care

of Power Boilers , Section VII of the ASME Boiler and Pressure Vessel Code, 1995.

Steam Tip Sheet information is adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-10099-954 • Revised October 2003 • Steam Tip Sheet #9 ◆ 

### Suggested Actions ◆ Review your blowdown practices to identify energy saving opportunities. Examine operating practices for boiler feedwater and bl owdown rates developed by the American Society of Mechanical Engineers (ASME). Considerations include operating pressure, steam purity, and deposition control. Consider an automatic blowdown control system (see sidebar). 

### Appendix B: Steam Tip Sheet Number 9

# Recover Heat from Boiler Blowdown

Heat can be recovered from boiler blowdown by using a heat exchanger to preheat boiler makeup water. Any boiler with continuous blowdown exceeding 5% of the steam rate is a good candidate for the introduction of blowdown wasteheat recovery. Larger energy savings occur with high-pressure boilers. The following table shows the potential for heat recovery from boiler blowdown.

◆ 

### Example In a plant where the fuel cost is $3.00/MMBtu, a continuous blowdown rate of3,200 pounds per hour (lbs/hr) is maintained to avoid the buildup of high concentrations of dissolved solids. What are the annual savings if a makeup water heat exchanger is installed that recovers 90% of the blowdown energy losses? The 82% efficient boiler produces 50,000 lbs/hr of 150-psig steam. It operates for 8000 hours per year. The blowdown ratio is:

Blowdown Ratio = 3200 = 6.0% 3200 + 50,000 From the table, the heat recoverable corresponding to a 6% blowdown ratio with a 150-psig boiler operating pressure is 1.8 MMBtu/hr. Since the table is based on a steam production rate of 100,000 lbs/hour, the annual savings for this plant are:

Annual Energy = 1.67 MMBtu/hr x (50,000 lbs/hr/100,000 lbs/hr) x 8000 hrs/yr = 8146 MMBtu Savings 0.82

Annual Cost Savings = 8146 MMBtu/year x $3.00/MMBtu = $24,438



### 70 Improving Steam System Performance Steam Tip Sheet information is adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-10099-955 • Revised June 2001 • Steam Tip Sheet #10 

### Blowdown Energy Recovery

Blowdown waste heat can berecovered with a heat exchanger, a flash tank, or flash tank in combination with a heatexchanger. Lowering the pressure in a flash tank allows a portion of the blowdown to be converted into low pressure steam. This low pressure steamis most typically used in deaerators. Drain water from the flash tank is then routed through a heat exchanger. Cooling the blowdown has the additional advantage of helping to comply with local codes limiting the discharge of high temperature liquids into the sewer system. Blowndown Heat Recovered, Million Btu per hour (MMBtu/hr) Rate, Boiler Operating Pressure, psig % Boiler Feedwater 50 100 150 250 300
2 0.45 0.5 0.55 0.65 0.65
4 0.9 1.0 1.1 1.3 1.3
6 1.3 1.5 1.7 1.9 2.0
8 1.7 2.0 2.2 2.6 2.7
10 2.2 2.5 2.8 3.2 3.3
20 4.4 5.0 5.6 6.4 6.6 Based on a steam production rate of 100,000 pounds per hour, 60°F makeup water, and 90% heat recovery.

◆ 

### Suggested Actions ◆ If there is a continuous blowdown system in place, consider installing a heat recovery system. If there is a non-continuous blowdown system, then consider the option of converting it to a continuous blowdown system coupled with heat recovery. 

### Appendix B: Steam Tip Sheet Number 10

Recoverable Heat from Boiler Blowdown

### 71 A Sourcebook for Industry 

# Use Vapor Recompression to Recover Low-Pressure Waste Steam

Low-pressure steam exhaust from industrial operations such as evaporators or cookers is usually vented to the atmosphere or condensed in a cooling tower. Simultaneously, other plant operations may require intermediate-pressure steamat 20 to 50 pounds per square inch gauge (psig). Instead of letting down highpressure steam across a throttling valve to meet these needs, low-pressure waste steam can be mechanically compressed or boosted to a higher pressure so that it can be reused.

Vapor recompression relies upon a mechanical compressor or steam jet ejector to increase the temperature of the latent heat in steam to render it usable for process duties. Recompression typically requires only 5% to 10% of the energy required to raise an equivalent amount of steam in a boiler.

◆ 

### Example Consider a petrochemical plant that vents 15-psig steam to the atmosphere. At the same time, a process imposes a continuous requirement on the boiler for 5,000 lbs/hr of 40-psig steam. If 15-psig waste steam is recompressed to 40 psig by an electrically driven compressor, the compression ratio is:

Compression Ratio = (40 + 14.7) / (15 + 14.7) = 1.84

From the table above, the compressor requires 63.5 Btu/lb of delivered steam. Assuming that electricity is priced at $0.05/kWh, the annual cost of driving the compressor is:

Compressor = 63.5 Btu/lb x 5,000 lbs/hr x 8,760 hrs/yr x $0.05/kWh / 3413 Btu/kWh Operating Cost = $40,745/year

If an equivalent quantity of 40-psig steam (enthalpy for saturated steam is 1176 Btu/lb) were to be supplied by an 82% efficient natural-gas-fired boiler, the steam production costs with fuel priced at $4.50/MMBtu and 70°F feedwater (enthalpy is 38 Btu/lb), are:

Steam = 5,000 lbs/year x (1176-38 Btu/lb) x 8,760 hrs/yr x $4.50/MMBtu / 0.82 Production Costs = $273,536/year

An nual Vapor Recompression Cost Savings = $273,536 - $40,745 = $232,791 

### Conduct a Pinch Analysis Based on the actual application, there may be other options to vapor recompres sion. The industry best practice is to conduct a pinch analysis on the steam system to reveal cost-effective alternatives andoptimize steam use by eliminating inefficiencies.



### Vapor Recompression Limits Vapor recompression is limited to applications where the compressor inlet pressure is above atmospheric and the compression ratio is less than two per stage.



### System Pressure Boosting Vapor recompression can be used in steam distribution systems to boost system pressures that have dropped to unacceptably low levels. Compressor Work, Btu/lb of Steam Produced
Inlet Compression Ratio Pressure (psig) 1.2 1.4 1.6 1.8 2.0
0 17.8 33.2 46.8 58.8 69.6
15 18.6 34.7 48.7 61.2 72.6 Assuming adiabatic compression with a compressor efficiency of 75 percent. 80°F water is sprayed into the steam to eliminate superheat.

Energy Required for Steam Recompression 

### Appendix B: Steam Tip Sheet Number 11

### 72 Improving Steam System Performance 

### Appendix B: Steam Tip Sheet Number 11 (continued)

◆ 

### Suggested Actions ◆ A vapor recompression project analysis consists of matching recovered waste heat with the need for low-pressure steam for proce ss or space heating. To perform this analysis: • Conduct a plant audit to identify sources of low-pressure waste steam • Estimate the heat recovery potential • Inventory all steam-utilizing equipment and list pressure requirements, energy consumption, and patterns of use • Estimate the cost-effectiveness of installing recompression equipment and connecting piping.

Steam Tip Sheet information is adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102001-1274 • May 2001 • Steam Tip Sheet #11

# Flash High-Pressure Condensate to Regenerate Low-Pressure Steam

Low-pressure process steam requirements are usually met by throttling highpressure steam, but a portion of the process requirements can be achieved at low cost by flashing high-pressure condensate. Flashing is particularly attractive when it is not economically feasible to return the high-pressure condensate to the boiler. In the table below, the quantity of steam obtained per pound of condensate flashed is given as a function of both condensate and steam pressures.

◆ 

### Example In a plant where the cost of steam is $4.50 per million Btu (MMBtu), saturated steam at 150 pounds per square inch gauge (psig) is generated, and a portion of it throttled to supply 30-psig steam. Assuming continuous operation, determine the annual energy savings of producing low-pressure steam by flashing 5,000 pounds per hour of 150-psig condensate. The average temperature of the boiler make-up water is 70°F.

From the table above, when 150-psig condensate is flashed at 30 psig, 10.3% of the condensate vaporizes.

Low-Pressure Steam Produced = 5,000 lbs/hr x 0.103 = 515 lbs/hr

From the ASME Steam Tables, the enthalpy values are:

For 30-psig saturated steam = 1171.9 Btu/lb For 70°F makeup water = 38.0 Btu/lb

Annual savings are obtained as follows:

Annual = 515 lb/hr x (1171.9–38.0) Btu/lb x 8,760 hours/year x $4.50/MMBtu Savings = $23,019 High Pressure Percent of Condensate Flashed, lb Steam/lb Condensate
Condensate Low-Pressure Steam (psig) (psig) 50 30 15 5
200 10.4 12.8 15.2 17.3
150 7.8 10.3 12.7 14.9
100 4.6 7.1 9.6 11.8
75 2.5 5.1 7.6 9.9 

### Proximity Is a Plus The source of high-pressurecondensate should be relatively close to the low-pressure steam header to minimize piping and insulation costs.



### Match Availability and Use
The economics of heat recovery projects are most favorable when the waste steam heat content is high and the flow is continuous. Seasonal space heating is not the most desirable end use.



### 73 A Sourcebook for Industry 

### Appendix B: Steam Tip Sheet Number 12

◆ 

### Suggested Actions ◆ Determine the potential for high-pressure condensate flashing by completing a plant survey that: • Identifies all sources of high-pressure condensate • Determines condensate flow and duration, as well as the heat recovery potential due to flashed steam production • Identifies compatible uses for low-pressure steam • Estimates the cost effectiveness of installing appropriate heat-recovery devices and interconnecting piping. High-Pressure Condensate Flashing

### 74 Improving Steam System Performance 

### Appendix B: Steam Tip Sheet Number 12 (continued)

Steam Tip Sheet information is adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102001-1275 • May 2001 • Steam Tip Sheet #12

### 75 A Sourcebook for Industry 

### Appendix B: Steam Tip Sheet Number 13


# Use a Vent Condenser to Recover Flash Steam Energy

When the pressure of saturated condensate is reduced, a portion of the liquid “flashes” to low-pressure steam. Depending on the pressures involved, the flash steam contains approximately 10% to 40% of the energy content of the original condensate. In most cases, including condensate receivers and deaerators, the flashing steam is vented and its energy content lost. However, a heat exchanger can be placed in the vent to recover this energy. The following table indicates the energy content of flash steam at atmospheric pressure.

◆ 

### Example Consider a vent pipe with the following conditions: Velocity of flash steam: 300 feet per minute Diameter of vent pipe: 4 inches Hours of operation: 8,000 hours per year Boiler efficiency: 82% Cost of fuel: $4.50 per million Btu (MMBtu)

A vent condenser could condense the flashed steam, transfer its thermal energy to incoming make-up water, and then return it to the boiler. Energy is recovered in two forms: hotter make-up water and clean, distilled condensate ready for productive use in your operation.

Referring to the table above, the potential energy recovered from the flashed steam is 555 MMBtu, based on 8,760 hours of annual operation. Correct this value for actual operating hours and boiler efficiency:

Annual Energy = 555 MMBtu/year x 8,000 hrs/yr / 8,760 hrs/yr x 1 / 0.82 Recovered = 618 MMBtu

Annual Potential = 618 MMBtu/yr x $4.50/MMBtu Fuel Cost Savings = $2,781**

** Note that the annual fuel savings are per vent. Often, there are several such vents in a

steam facility, and the total savings can be a significantly larger number. The additional heat exchanger cost still needs to be considered, but available literature shows a quick payback for the measure. 

### Distilled Water Recovery
A useful rule of thumb is that every 500 lbs/hr of recovered flash steam provides 1 gallon per minute (gpm) of distilled water.



### Materials Considerations Depending on the specific application, the vent condenser materials can be either all stainless or mild steel shell with copper tubes. For deaerator vent condensing, a stainlesssteel heat exchanger is recommended to avoid corrosion due to the high concentrations of gases. Mild steel can be used for receiver tank vent condensing. Pipe Energy Content. MMBtu/year*
Diameter Steam Velocity, feet/min (inches) 200 300 400 500 600
2 90 140 185 230 280 4 370 555 740 925 1,110 6 835 1,250 1,665 2,085 2,500 10 2,315 3,470 4,630 5,875 6,945 * Assumes continuous operation, 70°F make-up water, and condensed steam at 100°F.

Energy Recovery Potential of a Vent Condenser

### 76 Improving Steam System Performance 

### Appendix B: Steam Tip Sheet Number 13 (continued)

◆ 

### Suggested Actions ◆ • Inspect vent pipes of receiver tanks and deaerators for excessive flash steam plumes • Re-examine deaerator steam requirements • Eliminate remaining flash steam energy loss with a vent condenser • Consult manufacturers for materials specifications, as well as size and cost recommendations for the vent condenser.

Steam Tip Sheet information is adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102001-1276 • May 2001 • Steam Tip Sheet #13

# Use Low-Grade Waste Steam to Power Absorption Chillers

Absorption chillers use heat, instead of mechanical energy, to provide cooling. The mechanical vapor compressor is replaced by a thermal compressor (see figure) that consists of an absorber, a generator, a pump, and a throttling device. The refrigerant vapor from the evaporator is absorbed by a solution mixture in the absorber. This solution is then pumped to the generator where the refrigerant is revaporized using a waste steam heat source. The refrigerant-depleted solution is then returned to the absorber via a throttling device. The two most common refrigerant/absorbent mixtures used in absorption chillers are water/lithium bromide and ammonia/water.

Compared to mechanical chillers, absorption chillers have a low coefficient of performance (COP = chiller load/heat input). Nonetheless, they can substantially reduce operating costs because they are energized by low-grade waste heat, while vapor compression chillers must be motor- or engine-driven.

Low-pressure, steam-driven absorption chillers are available in capacities ranging from 100 to 1,500 tons. Absorption chillers come in two commercially available designs: single-effect and double-effect. Single-effect machines provide a thermal COP of 0.7 and require about 18 pounds of 15-psig steam per ton-hour of cooling. Double-effect machines are about 40% more efficient, but require a higher grade of thermal input, using about 10 pounds of 100- to 150-psig steam per ton-hour.

◆ 

### ExampleIn a plant where low-pressure steam is currently being exhausted to the atmosphere, a mechanical chiller with a COP of 4.0 is used 4,000 hours per year to produce an average of 300 tons of refrigeration. The cost of electricity at the plant is $0.05 per kilowatt-hour. 

### Reduce Demand Charges Absorption chillers can reshape facility thermal and electricload profiles by shifting cooling from an electric to a thermal load. If you are served by an electric utility with a ratcheted demand charge, you may be able to reduce demand charges throughout the year by reducing your summer peak loads.



### Utility Incentives Some gas utilities offer reduced rates during the summer. In some areas, electric utilities provide rebates or incentives to replace mechanical chillers with steam absorption units.



### 77 A Sourcebook for Industry 

### Appendix B: Steam Tip Sheet Number 14

* The evaporator and the condenser, required for both systems, are not shown in the figure. Mechanical Vapor Compression Thermal Vapor Compression Electric/EngineDriven Compressor High Pressure

Low Pressure Waste Heat from Process or Low-Pressure Steam

Pump Throttle Valve

Rejected Heat Refrigerant Vapor to Condenser

Refrigerant Vapor from Evaporator Refrigerant Vapor to Condenser

Refrigerant Vapor from Evaporator Generator

Absorber Comparison of Mechanical and Thermal Vapor Compression Systems*

### 78 Improving Steam System Performance 

### Appendix B: Steam Tip Sheet Number 14 (continued)

An absorption unit requiring 5,400 lbs/hr of 15-psig steam could replace the mechanical chiller, providing annual electrical cost savings of:

Annual = 300 tons x (12,000 Btu/ton / 4.0) x 4,000 hrs/year x $0.05/kWh x kWh/3,413 Btu Savings = $52,740

◆ 

### Suggested Actions ◆

Determine the cost-effectiveness of displacing a portion of your cooling load with a waste steam absorption chiller by taking the following steps: • Conduct a plant survey to identify sources and availability of waste steam • Determine cooling load requirements and the cost of meeting those requirements with existing mechanical chillers or new instal lations • Obtain installed cost quotes for a waste steam absorption chiller • Conduct a life cycle cost analysis to determine if the waste steam absorption chiller meets your company’s cost-effectiveness criteria.

Steam Tip Sheet information is adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102001-1277 • May 2001 • Steam Tip Sheet #14

# Benchmark the Fuel Cost of Steam Generation

Benchmarking the fuel cost of steam generation ($/1000 lbs of steam) is aneffective way to assess the efficiency of your steam system. This cost is dependent upon fuel type, unit fuel cost, boiler efficiency, feedwater temperature, and steam pressure. This calculation provides a good first approximation for the cost of generating steam and serves as a tracking device to allow for boiler performance monitoring. Table 1 shows the heat input required to produce one pound of saturated steam at different operating pressures and varying feedwater temperatures. Table 2 lists the typical energy content and boiler combustion efficiency for several common fuels.

Data from the above tables can be used to determine the cost of usable heat from a boiler or other combustion unit. The calculations can also include operating costs of accessories such as feedwater pumps, fans, fuel heaters, steam for fuel atomizers and soot blowing, treatment chemicals, and environmental and maintenance costs.

◆ 

### Example A boiler, fired with natural gas costing $0.30/therm, produces 450 psig saturatedsteam and is supplied with 230°F feedwater. Using values from the tables, calculate the cost of producing steam.

Steam Cost = 0.3 ($/therm) x 1000 x 1006 (Btu/lb) x 100 = $3.69/1000 lbs 100,000 (Btu/therm) 81.7 

### Effective Cost of Steam
The effective cost of steam depends on the path it follows from the boiler to the point of use. Take a systems approach and consider the entire boiler island, including effect of blowdown, parasitic steam consumption, deaeration, etc. Further complications arise due to the process steam loads at different pressures, multipleboilers, and waste heat recovery systems. To determine the effective cost of steam, use a combined heat and power simulation model that includes all the significant effects.



### Multi-Fuel Capability For multi-fuel capability boilers, take advantage of volatility in fuel prices by periodicallyanalyzing the steam generation cost and use the fuel that provides the lowest steam generation cost.



### Higher Versus Lower Heating Values Fuel is sold based on its gross or higher heating value (HHV). If, at the end of the combustion process, water remains in the form of vapor, the HHV must be reduced by the latent heat of vaporization of water. This reduced value is known as the lower heating value (LHV). Operating Feedwater Temperature, °F Pressure, psig 50 100 150 200 250 150 1,178 1,128 1,078 1,028 977 450 1,187 1,137 1,087 1,037 986 600 1,184 1,134 1,084 1,034 984 * Calculated from steam tables based on the difference between the enthalpies of saturated steam and feedwater.

Table 1. Energy Required to Produce One Pound of Saturated Steam (Btu)*



### 79 A Sourcebook for Industry 

### Appendix B: Steam Tip Sheet Number 15

Fuel Type Energy Content Combustion (sales unit) (Btu/sales unit) Efficiency (%) Natural Gas (therm) 100,000 81.7 Natural Gas (cubic foot) 1,030 81.7 Distillate/No. 2 Oil (gallon) 138,700 84.6 Residual/No. 6 Oil (gallon) 149,700 86.1 Coal (ton) 27,000,000 87.6 Note: Combustion efficiency is based on boilers equipped with economizers and air preheaters and 3% oxygen in flue gas.

Table 2. Energy Content and Combustion Efficiency of Fuels

### 80 Improving Steam System Performance 

### Appendix B: Steam Tip Sheet Number 15 (continued)

Steam Tip Sheet information is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102000-1115 • December 2000 • Steam Tip Sheet #15 ◆ 

### Suggested Actions ◆ • Determine your annual fuel costs based on utility bills. • Install a steam flowmeter in your facility and calculate your steam generation cost. Compare this with the benchmark value. • Using a systems approach, do a thermoeconomic analysis to determine the effective cost of steam. (See sidebar: Effective Cost

of Steam)

# Minimize Boiler Short Cycling Losses

Boiler "short cycling" occurs when an oversized boiler quickly satisfies process or space heating demands, and then shuts down until heat is again required. Process heating demands can change over time. Boilers may have been oversized for additions or expansions that never occurred. Installing energy conservation or heat recovery measures may also reduce the heat demand. As a result, a facility may have multiple boilers, each rated at several times the maximum expected load.

Boilers used for space heating loads are often oversized, with their capacity chosen to meet total building heat losses plus heating of ventilation and infiltration air under extreme or design-basis temperature conditions. No credit is taken for thermal contributions from lights, equipment, or people. Excess capacity is also added to bring a facility to required settings quickly after a night setback.

◆ 

### Cycling Losses A boiler cycle consists of a firing interval, a post-purge, an idle period, a pre-purge, and a return to firing. Boiler efficiency is the useful heat provided by the boiler divided by the energy input (useful heat plus losses) over the cycle duration. This efficiency decreases when short cycling occurs or when multiple boilers are operated at low-firing rates.

This decrease in efficiency occurs, in part, because fixed losses are magnified under lightly loaded conditions. For example, if the radiation loss from the boiler enclosure is 1% of the total heat input at full-load, at half-load the losses increase to 2%, while at one-quarter load the loss is 4%. In addition to radiation losses, pre- and post-purge losses occur. In the pre-purge, the fan operates to force air through the boiler to flush out any combustible gas mixture that may have accumulated. The post-purge performs a similar function. During purging, heat is removed from the boiler as the purged air is heated.

◆ 

### Example A 1,500 hp (1 hp = 33,475 Btu/hr) boiler with a cycle efficiency of 72.7% (E 1 ) is replaced with a 600 hp boiler with a cycle efficiency of 78.8% (E 2). Calculate the annual cost savings.

Fractional Fuel Savings = (1 – E 1 /E 2) = (1 – 72.7/78.8) x 100 = 7.7%

If the original boiler used 200,000 MMBtu of fuel annually, the savings from switching to the smaller boiler (given a fuel cost of $3.00/MMBtu) are:

Annual Savings = 200,000 MMBtu x 0.077 x $3.00/MMBtu = $46,200 

### Multiple Boiler Operations
The most efficient boilers should be brought on-line as loads increase, with less-efficient units taken off-line first as loads drop. Subject to emissions, operations, or firing rate limits, shift loadsfrom a boiler where steam production is expensive to one where it is less expensive.

Use automatic controllers that determine the incremental costs (change in steam cost/ change in load) for each boiler in the facility, and then shiftloads accordingly. This maximizes efficiency and reduces energy costs. If possible, scheduleloads to help optimize boiler system performance. Powerhouses containing multiple boilersthat are simultaneously operated at low-fire conditions offer energy-saving opportunities by using proper boiler allocation strategies.



### Boiler Downsizing Fuel savings can be achieved by adding a smaller boiler sized to meet average loads at your facility, or by re-engineering the power plant to consist of multiple small boilers. Multiple small boilers offer reliability and flexibility to operators to follow load swings without over-firing and short cycling. Facilities with large seasonal variations in steam use operate small boilers when demand drops rather than operating their large boilers year-round.



### 81 A Sourcebook for Industry 

### Appendix B: Steam Tip Sheet Number 16

Steam Tip Sheet information is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102000-1116 • December 2000 • Steam Tip Sheet #16 ◆ 

### Suggested Actions ◆ • Determine the efficiency and operating cost of each of your boilers and adopt a control strategy for maximizing overall effici ency of

multiple boiler operations. (See sidebar) • Avoid short cycling by adding small boilers to your boiler facility to provide better flexibility and high efficiency at all l oads. (See

sidebar: Boiler Downsizing)

### 82 Improving Steam System Performance

# Install Removable Insulation on Valves and Fittings

During maintenance, the insulation that covers pipes, valves, and fittings is often damaged or removed and not replaced. Pipes, valves, and fittings that are not insulated can be safety hazards and sources of heat loss. Removable and reusable insulating pads are available to cover almost any surface. The pads aremade of a noncombustible inside cover, insulation material, and a noncombustible outside cover that resists tears and abrasion. Material used in the pads resists oil and water and has been designed for temperatures of up to 1600°F. Wire laced through grommets or straps with buckles hold the pads in place.

◆ 

### Applications Reusable insulating pads are commonly used in industrial facilities for insulating flanges, valves, expansion joints, heat exchangers, pumps, turbines, tanks, and other irregular surfaces. The pads are flexible and vibration resistant and can be used with equipment that is horizontally or vertically mounted or that is difficult to access. Any high-temperature piping or equipment should be insulated to reduce heat loss, reduce emissions, and improve safety. As a general rule, anysurface that reaches temperatures greater than 120°F should be insulated to protect personnel. Insulating pads can be easily removed for periodic inspection or maintenance, and replaced as needed. Insulating pads can also contain built-in acoustical barriers to help control noise.

◆ 

### Energy Savings The table below summarizes energy savings due to the use of insulating valve covers for a range of valve sizes and operating temperatures. These values were calculated using a computer program that meets the requirements of ASTM C 680—Heat Loss and Surface Temperature Calculations . The energy savings is defined as the difference in heat loss between the uninsulated valve and the insulated valve operating at the same temperature.

◆ 

### Example Using the table above, calculate the annual fuel and dollar savings from installing a 1-inch thick insulating pad on an uninsulated 6-inch gate valve in a 250 pounds per square inch gauge (psig) saturated steam line (406°F). Assume continuous operation with natural gas at a boiler efficiency of 80% and a fuel price of $4.50 per million British thermal units (MMBtu). 

### Availability Insulation supply companies are located regionally; this expedites delivery and helpsmeet site-specific job requirements. Most supply companies can take measurements on-siteto ensure the best fit on irregular surfaces. For customized applications, manufacturers can provide instructions regarding the installation and removal of insulating pads.



### Noise Control Benefits Specify insulating pads that contain built-in barriers for noise control.



### Insulation for Steam Traps Effectively insulate inverted bucket traps with removableand reusable snap-on insulation. Thermostatic traps and disk traps should be insulated according to manufacturers’ specifications to ensure proper operation.

Before removal of all or any existing insulation material,check for asbestos in accordance with OSHA regulations.



### 83 A Sourcebook for Industry 

### Appendix B: Steam Tip Sheet Number 17

Operating Valve Size (inches) Temperature, °F 3 4 6 8 10 12 200 800 1,090 1,560 2,200 2,900 3,300 300 1,710 2,300 3,300 4,800 6,200 7,200 400 2,900 3,400 5,800 8,300 10,800 12,500 500 4,500 6,200 9,000 13,000 16,900 19,700 600 6,700 9,100 13,300 19,200 25,200 29,300

a Based on installation of a 1-inch thick insulating pad on an ANSI 150-pound class flanged valve with an ambient

temperature of 65°F and zero wind speed. Energy Savings a from Installing Removable Insulated Valve Covers (Btu/hour)

### 84 Improving Steam System Performance 

### Appendix B: Steam Tip Sheet Number 17 (continued)

Results:

Annual Fuel Savings = 5,992 Btu/hr x 8,760 hours/year x 1/0.80 = 65.6 MMBtu/year

Annual Dollar Savings = 65.6 MMBtu/year x $4.50/MMBtu = $295 per 6-inch gate valve

Steam Tip Sheet information is adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102004-1802 • April 2004 • Steam Tip Sheet #17 ◆ 

### Suggested Actions ◆ • Conduct a survey of your steam distribution system to identify locations where removable and reusable insulation covers can beused • Use removable insulation on components requiring periodic inspections or repair.

### 85 A Sourcebook for Industry 

# Deaerators in Industrial Steam Systems

Deaerators are mechanical devices that remove dissolved gases from boiler feedwater. Deaeration protects the steam system from the effects of corrosive gases. It accomplishes this by reducing the concentration of dissolved oxygen and carbon dioxide to a level where corrosion is minimized. A dissolved oxygen level of 5 parts per billion (ppb) or lower is needed to prevent corrosion in most high pressure (>200 psig) boilers. While oxygen concentrations of up to 43 ppb may be tolerated in low pressure boilers, equipment life is extended at little or no cost by limiting the oxygen concentration to 5 ppb. Dissolved carbon dioxide is essentially completely removed by the deaerator.

◆ 

### How They Work The design of an effective deaeration system depends upon the amount of gases to be removed and the final gas (O 2) concentration desired. This in turn dependsupon the ratio of boiler feedwater makeup to returned condensate and the operating pressure of the deaerator.

Deaerators use steam to heat the water to the full saturation temperature corresponding to the steam pressure in the deaerator and to scrub out and carry away dissolved gases. Steam flow may be parallel, cross, or counter to the water flow. The deaerator consists of a deaeration section, a storage tank, and a vent. In the deaeration section, steam bubbles through the water, both heating and agitating it. Steam is cooled by incoming water and condensed at the vent condenser. Non-condensable gases and some steam are released through the vent.

Steam provided to the deaerator provides physical stripping action and heats themixture of returned condensate and boiler feedwater makeup to saturation temperature. Most of the steam will condense, but a small fraction (usually 5 to 14%) must be vented to accommodate the stripping requirements. Normal design practice is to calculate the steam required for heating, and then make sure that the flow is sufficient for stripping as well. If the condensate return rate ishigh (>80%) and the condensate pressure is high compared to the deaerator pressure, then very little steam is needed for heating, and provisions may be made for condensing the surplus flash steam.

◆ 

### Deaerator Steam ConsumptionThe deaerator steam consumption is equal to the steam required to heat incoming water to its saturation temperature, plus the amount vented with the noncondensable gases, less any flashed steam from hot condensate or steam losses through failed traps. The heat balance calculation is made with the incoming water at its lowest expected temperature. The vent rate is a function of deaeratortype, size (rated feedwater capacity), and the amount of makeup water. The operating vent rate is at its maximum with the introduction of cold, oxygen-rich makeup water. 

### Additional Benefits Deaerators provide the water storage capacity and the netpositive suction head necessary at the boiler feed pump inlet. Returned condensate is mixed with makeup waterwithin the deaerator. Operating temperatures range from 215°F to over 350°F, which reduces the thermal shock ondownstream preheating equipment and the boiler.



### Insulation
The deaerator section and storage tank and all piping conveying hot water or steam should be adequately insulated to prevent the condensation of steam and loss of heat.



### Function Clarification The deaerator is designed toremove oxygen that is dissolved in the entering water, not entrained air. Sources of “free air” include loose piping connections on the suction side of pumps and improper pump packing.



### Pressure Fluctuations
Sudden increases in free or “flash” steam can cause aspike in deaerator vessel pressure, resulting in re-oxgenation of the feedwater. A dedicated pressure-regulating valve should be provided to maintain the deaerator at a constant pressure.

Steam Tip Sheet information is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102000-1118 • December 2000 • Steam Tip Sheet #18 ◆ 

### Suggested Actions ◆ • Deaerator steam requirements should be re-examined following the retrofit of steam distribution system, condensate return, or he at

recovery energy conservation measures. • Install continuous dissolved oxygen monitoring devices to aid in identifying operating practices that result in poor oxygen re moval. 

### Appendix B: Steam Tip Sheet Number 18

# Cover Heated, Open Vessels

Open vessels that contain heated liquids often have a high heat loss due to surface evaporation. Both energy and liquid losses are reduced by covering open vessels with insulated lids. Table 1 provides an estimate of the evaporative heat loss per square foot of uncovered vessel surface area for various water and dry ambient air temperatures. It is assumed that the ambient air is dry with no wind currents. A fan pulling air over the uncovered tank could more than double the heat losses.

◆ 

### Example A rinse tank is four feet wide and ten feet long. It is maintained at a constant temperature of 170° F. Determine the evaporative heat loss from the tank if the ambient temperature is 75° F.

Area of Evaporating Surface = 4 ft x 10 ft = 40 ft 2 Total Heat Loss for Uncovered Liquid Surface = 1,566 Btu/hr-ft 2 x 40 ft 2 = 62,640 Btu/hr

◆ 

### Cover the Tank with an Insulated Top Assume that the rinse tank is heated during two shifts per day, five days per week, and 50 weeks per year. What are the annual energy savings that may be attained by covering the tank? What is the heating cost reduction in a plant where the cost of steam is $6.50/MMBtu? Assume that covering the rinse tank with an insulated lid effectively reduces the heat losses from the liquid surface to a negligible value.

Annual Energy Savings = 62,640 Btu/hr x 2 shifts/day x 8 hrs/shift x 250 days/yr = 250 MMBtu/yr Heating Cost Reduction = 250 MMBtu/yr x $6.50/MMBtu = $ 1,625/yr



### 86 Improving Steam System Performance 

### Appendix B: Steam Tip Sheet Number 19

Heat Loss Detail • Eliminating internal heat

gains will also result in electrical energy savings if the open tanks are located within a conditioned space.• Heat losses are a strong function of both wind velocity and ambient air humidity. A wind velocity of 3 miles per hour will more than double the rate of heat loss from a tank.
• Radiation heat transfer is a

secondary source of tank surface heat losses. Radiation losses increase from 90 Btu/hr-ft 2 at a liquid temperature of 110° F to 290 Btu/hr-ft 2 at 190° F.

Steam Tip Sheet information adapted from information provided by the Industrial Energy Extension Service of Georgia Tech and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102002-1477 • January 2002 • Steam Tip Sheet #19 ◆ 

### Suggested Actions ◆ • Conduct a survey to determine the number of open vessels that contain heated liquid within your plant. For each tank, determinethe

operating schedule, liquid temperature, ambient temperature, and the square feet of exposed area. • Estimate the annual heat loss from the uncovered tanks and determine the potential annual fuel cost savings. • Evaporation and heat losses can be reduced by lowering the liquid temperature, reducing the exposed liquid area, minimizing flowof

air over the tank, or by installing an insulated cover. • Obtain cost quotations for insulated covers. Install covers when they are economically justified. Note:Table 1 is extracted from “Steam Efficiency Improvement” by the Boiler Efficiency Institute at Auburn University Liquid Ambient Air Temperature, °F Temperature, °F 65 75 85 95 105
110 244 222 200 177 152
130 479 452 425 397 369
150 889 856 822 788 754 170 1,608 1,566 1,524 1,482 1,440 190 2,900 2,845 2,790 2,737 2,684 Table 1. Evaporative Heat Loss from Water in Open Tanks, Btu/hr-ft2

# Replace Pressure-Reducing Valves with Backpressure Turbogenerators

Many industrial facilities produce steam at a higher pressure than is demanded by process requirements. Steam passes through pressure-reducing valves (PRVs, also known as letdown valves) at various locations in the steam distribution system to let down or reduce its pressure. A non-condensing or backpressure steam turbine can perform the same pressure-reducing function as a PRV, while converting steam energy into electrical energy.

In a backpressure steam turbogenerator, shaft power is produced when a nozzle directs jets of high-pressure steam against the blades of the turbine’s rotor. The rotor is attached to a shaft that is coupled to an electrical generator. The steam turbine does not consume steam. It simply reduces the pressure of the steam that is subsequently exhausted into the process header.

◆ 

### Cost-Effective Power Generation In a conventional, power-only steam turbine installation, designers increaseefficiency by maximizing the pressure drop across the turbine. Modern Rankinecycle power plants with 1,800 psig superheated steam boilers and condensing turbines exhausting at near-vacuum pressures can generate electricity with efficiencies of approximately 40%.

Most steam users do not have the benefit of ultra-high-pressure boilers and cannot achieve such high levels of generation efficiency. However, by replacing a PRV with a backpressure steam turbine, where the exhaust steam is provided to aplant process, energy in the inlet steam can be effectively removed and converted into electricity. This means the exhaust steam has a lower temperature than it would have if its pressure was reduced through a PRV. In order to make up for this heat loss, steam plants with backpressure turbine installations increase their boiler steam throughput.

Thermodynamically, the steam turbine still behaves the same way as it would in a conventional Rankine power cycle, achieving isentropic efficiencies of 20% to 70%. Economically, however, the turbine generates power at the efficiency of your steam boiler (modern steam boilers operate at approximately 80% efficiency), which then must be replaced with an equivalent kWh of heat for downstream purposes. The resulting power generation efficiencies are well in excess of the average U.S. electricity grid generating efficiency of 33%. Greater efficiency means less fuel consumption; backpressure turbines can produce power at costs that are often less than 3 cents/kWh. Energy savings are often sufficient to completely recover the cost of the initial capital outlay in less than 2 years.

◆ 

### Applicability Packaged or “off-the-shelf” backpressure turbogenerators are now available in ratings as low as 50 kW. Backpressure turbogenerators should be considered when a PRV has constant steam flows of at least 3,000 lbs/hr, and when the steam pressure drop is at least 100 psi. The backpressure turbine is generally installed in parallel with the PRV.

◆ 

### Estimating Your Savings To make a preliminary estimate of the cost of producing electrical energy from a back-pressure steam turbine, divide your boiler fuel cost (in $/MMBtu) by your boiler efficiency. Then convert the resulting number into cost per kWh, as shown 

### Life and Cost of Backpressure Turbogenerators Turbogenerators with electrical switchgear cost about $700/kW for a 50 kW system to less than $200/kW for a 2,000 kW system. Installation cost varies, but typically averages 75% of equipment costs.

Backpressure steam turbines are designed for a 20-year minimum service life and are known for needing low maintenance.



### 87 A Sourcebook for Industry 

### Appendix B: Steam Tip Sheet Number 20

### 88 Improving Steam System Performance 

### Appendix B: Steam Tip Sheet Number 20 (continued)

in the sample calculation.

Electricity cost = Fuel cost ($/MMBtu) x 0.003412 MMBtu/kWh Boiler efficiency

Example: $5.00/MMBtu x 0.003412 MMBtu/kWh = $0.021/kWh 0.80 To estimate the potential power output at a PRV, refer to Figure 1, which shows lines of constant power output (expressed in kW of electrical output per 1,000 pounds per hour of steam throughput) as a function of turbine inlet and exhaust pressures. Look up your input and output pressure on the horizontal and vertical axes, and then use the reference lines to estimate the backpressure turbogenerator power output per Mlb-hour of steam flow. Then estimate the total installed generating capacity (kW) by multiplying this number by your known steam flow rate. The annual cost savings from the backpressure turbine can then be estimated as:

Power output (kW) x Steam duty (hrs/year) x (Cost of grid power – Cost of generated power, $/kWh)

◆ 

### Suggested Actions ◆ Consider replacing PRVs with backpressure turbogenerators when purchasing new boilers or if your boiler operates at a pressure of 150 psig or greater. • Develop a current steam balance and actual process pressure requirements for your plant • Develop steam flow/duration curves for each PRV station • Determine plant electricity, fuel cost, and operating voltage • Consider either one centralized turbogenerator, or multiple turbogenerators at PRV stations.

Steam Tip Sheet information is adapted from material provided by the TurboSteam Corporation and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102002-1476 • January 2002 • Steam Tip Sheet #20 Note: Assumes a 50% isentropic turbine efficiency, a 96% efficient generator, and dry saturated inlet steam 300

250

200

150

100

50

0 100 200 300 400 500 600 700 800 10 kW/Mlb-hour

18 kW/Mlb-hour

25 kW/Mlb-hour

Input Pressure (psig)Exhaust Pressure (psig) Figure 1. Backpressure Turbogenerator Generating Potential (kW/Mlb-hour)

# Consider Steam Turbine Drives for Rotating Equipment

Steam turbines are well suited as prime movers for driving boiler feedwater pumps,forced or induced-draft fans, blowers, air compressors, and other rotating equipment. This service generally calls for a backpressure non-condensing steam turbine. The low-pressure steam turbine exhaust is available for feedwater heating, preheating of deaerator makeup water, and/or process requirements.

Steam turbine drives are equipped with throttling valves or nozzle governors to modulate steam flow and achieve variable speed operation. The steam turbine drive is thus capable of serving the same function as an induction motor coupled to an inverter or adjustable speed drive. Steam turbine drives can operate over a broad speed range and do not fail when overloaded. They also exhibit the high starting torque required for constant torque loads such as positive displacement pumps.

Steam turbines are inherently rugged and reliable low-maintenance devices. They are easy to control and offer enclosed, non-sparking operation suitable for use in explosive atmospheres or highly corrosive environments. Steam turbines provide fast, reliable starting capability and are particularly adaptable for direct connection to equipment that rotates at high speeds. Steam turbine drives may be installed for continuous duty under severe operating conditions, or used for load shaping (e.g. demand limiting), standby, or emergency service.

Steam turbine performance is expressed in terms of isentropic efficiency or steam rate (the steam requirement of the turbine per unit of shaft power produced). Steam rates are given in terms of pounds per horsepower-hour (lb/hp-hour) or lb/kWh.

◆ 

### Example A 300-hp steam turbine has an isentropic efficiency of 43% and a steam rate of 26 lb/hp-hour given the introduction of 600 psig/750°F steam with a 40 psig/486°F exhaust. What steam flow is necessary to replace a fully-loaded 300- hp feedwater pump drive motor?

Steam flow = 26 lb/hp-hr x 300 hp = 7,800 lb/hr

An examination of the ASME steam tables reveals that this steam turbine would utilize 103 Btu/lb of steam or 0.80 MMBtu of thermal energy per hour. Given a natural gas cost of $5.00/MMBtu and a boiler efficiency of 80%, the fuel-related cost of steam turbine operation is (0.80 MMBtu/hr/0.80 x $5.00/MMBtu) = $5.00/hr.

In comparison, a 300-hp motor with a full-load efficiency of 95% would require:
300 hp x (0.746 kW/hp) = 235.6 kWh/hr 0.95

In this example, the steam turbine drive would provide energy cost savings when the price of electricity exceeds:

$5.00/hr x 100 cents/$ = 2.12 cents/kWh 235.6 kWh/hr The total annual energy savings are strongly dependent upon the facility energy 

### Steam Turbine Flexibility Equipment redundancy and improved reliability can be obtained by mounting a steam turbine drive and an electric motor on opposite ends of the driven-equipment shaft. You can then select either the motor or turbine as the prime mover by increasing or decreasing the turbine speed relative to the synchronous speed of the motor.



### 89 A Sourcebook for Industry 

### Appendix B: Steam Tip Sheet Number 21

### 90 Improving Steam System Performance 

### Appendix B: Steam Tip Sheet Number 21 (continued)

cost and the hours per year of feedwater pump operation. Annual energy savings are given in Table 1 for various electrical rates and pump operating schedules. In addition to operating cost savings, steam turbine maintenance costs should be compared with electric motor maintenance expenses.

◆ 

### Suggested Actions ◆ Consider replacing electric motors with steam turbine drives if your facility: • Contains a high-pressure boiler or a boiler designed to operate at a higher pressure than process requirements • Has time-of-use (e.g., on/off peak, real-time, etc.) energy purchase and resale contracts with periods when electric power costs are

substantially higher than fuel costs • Has pumps or other rotating equipment requiring variable speed operation • Requires continued equipment operation during electrical power supply interruptions.

Steam Tip Sheet information is adapted from material provided by the TurboSteam Corporation and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102002-1475 • January 2002 • Steam Tip Sheet #21 1 Savings are based upon operation of a 300-hp steam turbine drive with a steam rate of 26 lbs/hp-hr.

A natural gas cost of $5.00/MMBtu is assumed. Electricity Feedwater Pump Annual Operating Hours Costs, $/kWh 2,000 4,000 6,000 7,000 8,760 0.03 $4,105 $8,210 $12,310 $14,365 $17,975 0.05 $13,525 $27,050 $40,570 $47,330 $59,230 0.075 $25,305 $50,605 $75,910 $88,560 $110,830 Table 1. Annual Energy Savings When Using a Steam Turbine Feedwater Pump Drive 1

### 91 A Sourcebook for Industry 

# Consider Installing High-Pressure Boilers with Backpressure Turbine-Generators

When specifying a new boiler, consider a high-pressure boiler with a backpressure steam turbine-generator placed between the boiler and the steam distribution network. A turbine-generator can often produce enough electricity to justify the capital cost of purchasing the higher-pressure boiler and the turbine-generator.

Since boiler fuel usage per unit of steam production increases with boiler pressure, facilities often install boilers that produce steam at the lowest pressure consistent with end use and distribution requirements.

In the backpressure turbine configuration, the turbine does not consume steam.Instead, it simply reduces the pressure and energy content of steam that is subsequently exhausted into the process header. In essence, the turbo-generator serves the same steam function as a pressure-reducing valve (PRV)—it reduces steam pressure—but uses the pressure drop to produce highly valued electricity in addition to the low-pressure steam. Shaft power is produced when a nozzle directs jets of high-pressure steam against the blades of the turbine’s rotor. The rotor is attached to a shaft that is coupled to an electrical generator.

◆ 

### Cost Effective Power GenerationIn a backpressure steam turbine, energy from high-pressure inlet steam is efficiently converted into electricity and low-pressure exhaust steam is provided to a plant process. The turbine exhaust steam has a lower temperature than the superheated steam created when pressure is reduced through a PRV. In order to make up for this heat or enthalpy loss and meet process energy requirements, steam plants with backpressure turbine installations must increase their boilersteam throughput (typically by 5%-7%). Every Btu that is recovered as highvalue electricity is replaced with an equivalent Btu of heat for downstream processes.
Thermodynamically, steam turbines achieve an isentropic efficiency of 20%-70%. Economically, however, the turbine generates power at the efficiency of the steam boiler. The resulting power generation efficiency (modern steam boilers operate at approximately 80% efficiency) is well in excess of the efficiency for state-of-the-art single or combined cycle gas turbines. High efficiency means low electricity generating costs. Backpressure turbines can produce electrical energy at costs that are often less than 3 cents/kWh. The electricity savings alone—not to mention ancillary benefits from enhanced on-site electricity reliability andreduced emissions of CO2 and criteria pollutants—are often sufficient to completely recover the cost of the initial capital outlay in less than 2 years.

◆ 

### Estimating Your Savings Since you have already determined that you need a boiler to satisfy your processthermal loads, the marginal cost of power produced from the backpressure turbine-generator is:

Cost of power production = (Annual boiler fuel cost after pressure increase – Annual boiler fuel cost before pressure increase) / Annual kWh produced by turbine-generator 

### BackgroundThe capital cost of a back-pressure turbogenerator complete with electrical switchgear varies from about $700/kW for a small system (50 kW) to less than $200/kW for a larger system (>2,000 kW). Installation costs vary depending upon piping and wiring runs, but typically average 75% of equipment costs.

Packaged or “off-the-shelf” backpressure turbogenerators are now available in ratings as low as 50 kW. Backpressureturbogenerators should be considered when a boiler has steam flows of at least 3,000 lbs/hr, and when the steam pressure drop between the boiler and the distribution network is at least 100 psig. The backpressure turbine is generally installed in parallel with a PRV, to ensure that periodic turbine-generator maintenance does not interfere with plant thermal deliveries. 

### Appendix B: Steam Tip Sheet Number 22

### 92 Improving Steam System Performance 

### Appendix B: Steam Tip Sheet Number 22 (continued)

The cost of boiler fuel before and after a proposed pressure increase can be calculated directly from the boiler fuel cost, boiler efficiency, and inlet and outlet steam conditions. The annual kWh produced by the turbine generator can be calculated from the inlet and exhaust pressures at the turbine, along with the steam flow rate through the turbine, in thousand pounds per hour (Mlb/hour).

To estimate the potential power output of your system, refer to Figure 1, which shows lines of constant power output, expressed in kW of electricity output per Mlb/hour of steam throughput as a function of the inlet and exhaust pressure through the turbine. Look up your input and output pressure on the axes shown, and thenuse the lines provided to estimate the power output, per Mlb/hour of steam flow rate for a backpressure turbogenerator. You can then estimate the turbine power output by multiplying this number by your known steam flow rate.

◆ 

### Example A chemical company currently uses a 100-psig boiler with 78% boiler efficiency (hboiler) to produce 50,000pounds per hour (lb/hr) of saturated steam for process loads. The plant operates two shifts per day, with the boiler operating at rated capacity for 6,000 hours/year. The boiler has reached the end of its service life and the company is considering replacing the boiler with a new 100-psig boiler or with a high-pressure 600-psig boiler and a backpressure steam turbine-generator. Both new boiler alternatives have rated efficiencies of 80%. The company currently pays 6 cents/kWh for electricity, and purchases boiler fuel for $5.00/MMBtu. Condensate return to the boiler has an enthalpy of 150 Btu/lb. What are the relative financial merits of the two systems?

Step 1: Calculate the current annual boiler fuel cost = $2,000,000 per year

Current boiler fuel cost = [fuel price] x [steam rate] x [annual operation] x [steam enthalpy gain] / [hboiler] = $5.00/MMBtu x 50,000 lb/hr x 6,000 hrs/yr x (1,190 Btu/lb – 150 Btu/lb) /0.78 = $2,000,000 per year

Step 2: Calculate the boiler fuel cost of a new 100-psig low-pressure (LP) boiler = $1,950,000 per year Resulting reductions in fuel costs are due solely to the higher efficiency of the new boiler.

New LP boiler fuel cost = [fuel price] x [steam rate] x [annual operation] x [steam enthalpy gain] / [hboiler] = $5.00/MMBtu x 50,000 lb/hr x 6,000 hrs/yr x (1,190 Btu/lb – 150 Btu/lb) /0.80 = $1,950,000 per year Note: Assumes 50% isentropic turbine efficiency, a 96% efficient generator, and dry unsaturated inlet steam. 10 kW per Mlb/hour

18 kW per Mlb/hour

25 kW per Mlb/hour

100 200 300 400 500 600 700 800 300

250

200

150

100

50

0

Input Pressure (psig)Exhaust Pressure (psig) Figure 1. Estimating Power Output Using Steam Inlet and Exhaust Pressures

### 93 A Sourcebook for Industry 

### Appendix B: Steam Tip Sheet Number 22 (continued)

Step 3: Calculate the boiler fuel cost of a new high-pressure (HP) boiler capable of producing 600-psig, 750°F superheated steam = $2,073,940 per year We must now take into account the additional enthalpy necessary to raise the pressure of the boiler steam to 600-psig. With a 50% isentropic turbine efficiency, the exhaust steam from the backpressure turbine is at 100-psig and 527°F and must be desuperheated. In order to provide an equivalent amount of thermal energy to the process loads, the boiler steam output is reduced to 45,000 lbs/hour.

New HP boiler fuel cost = [fuel price] x [steam rate] x [annual operation] x [steam enthalpy gain] / [hboiler] = $5.00/MMBtu x 45,000 lb/hr x 6,000 hrs/yr x (1,379 Btu/lb – 150 Btu/lb) / 0.80 = $2,073,940 per year

Step 4: Estimate the electricity output of the steam turbine-generator = 6,750,000 kWh/year At 600-psig inlet pressure with 750°F superheated steam and 100-psig exhaust pressure, the system will satisfyexisting steam loads, but will also produce approximately 25 kW of electric power per Mlb/hour of steam production (Refer to Figure 1 to estimate your power output for steam at saturated conditions). Thus,

Turbine-generator power output = 45 Mlb/hour x 25 kW/Mlb/hour = 1,125 kW

Assuming a 6,000-hour operating year, the electricity output of this turbine will be:

Turbine-generator electricity output = 1,125 kW x 6,000 hours/year = 6,750,000 kWh/year

Step 5: Determine the cost of electricity produced by the turbine = $0.018/kWh The value is derived from the difference in fuel costs between the two boiler alternatives, divided by the power produced by the turbine:

Fuel cost of produced electricity = [$2,073,940/year - $1,950,000/year] / 6,750,000 kWh/year = $0.018/kWh

Step 6: Calculate energy savings benefits = $283,500 per year

Cost savings = 1,125 kW x ($0.06/kWh – $0.018/kWh) x 6,000 hours per year = $283,500 per year

This level of savings is often more than adequate to justify the capital and maintenance expenditures for the backpressure turbine-generator set and the incremental cost of purchasing and installing the higher-pressure boiler.

◆ 

### Suggested Actions ◆ Consider installation of a high-pressure boiler with a backpressure turbine-generator whenever undertaking a boiler upgrade. Wh en evaluating this opportunity, you should: • Determine how much steam enthalpy, pressure and temperature is required at the header downstream from your boiler. • Calculate the incremental fuel cost between a low-pressure boiler and a high-pressure boiler. • Develop steam flow/duration curves for your boiler. (Remember that electrical generation will follow your steam load or proc ess

heating requirements). • Obtain plant electricity and fuel cost information. • Use the tools provided in this fact sheet to estimate your electricity generation potential and to determine savings from purc hasing

and installing a high-pressure boiler plus a backpressure turbine-generator set.

Steam Tip Sheet information is adapted from material provided by the TurboSteam Corporation and is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102004-1710 • July 2004 • Steam Tip Sheet #22

### 94 Improving Steam System Performance

# Install an Automatic Blowdown Control System

During the surface blowdown process, a controlled amount of boiler water containing high dissolved solids concentrations is discharged into the sewer. In addition to wasting water and chemicals, the blowdown process wastes heat energy,because the blowndown liquid is at the same temperature as the steam produced—approximately 366°F for 150 pounds per square inch gauge (psig) saturated steam—and blowdown heat recovery systems, if available, are not 100% efficient. (Waste heat may be recovered through the use of a blowdown heat exchanger or a flash tank in conjunction with a heat recovery system. For more information, see Steam Tip Sheet #10, Recover Heat from Boiler Blowdown).

◆ 

### Advantages of Automatic Control Systems With manual control of surface blowdown, there is no way to determine the concentration of dissolved solids in the boiler water, nor the optimal blowdown rate. Operators do not know when to blow down the boiler, nor for how long. Likewise, using a fixed rate of blowdown does not take into account changes in makeup and feedwater conditions, or variations in steam demand or condensate return.

An automatic blowdown-control system optimizes surface-blowdown rates by regulating the volume of water discharged from the boiler in relation to the concentration of dissolved solids present. Automatic surface-blowdown control systems maintain water chemistry within acceptable limits, while minimizing blowdown and reducing energy losses. Cost savings come from the significant reduction in consumption, disposal, treatment, and heating of water.

◆ 

### How it Works With an automatic blowdown-control system, high- or low-pressure probes are used to measure conductivity. The conductivity probes provide feedback to a blowdown controller that compares the measured conductivity with a set-point value, and then transmits an output signal that drives a modulating blowdown release valve.

Conductivity is a measure of the electrical current carried by positive and negative ions when a voltage is applied across electrodes in a water sample. Conductivity increases when the dissolved ion concentrations increase. The measured current is directly proportional to the specific conductivity of the fluid. Total dissolved solids (TDS), silica, chloride concentrations, and/or alkalinity contribute to conductivity measurements. These chemical species are reliable indicators of salts and other contaminates in the boiler water.

◆ 

### Applications Boilers without a blowdown heat-recovery system and with high blowdown ratesoffer the greatest energy-savings potential. The optimum blowdown rate is determined by a number of factors including boiler type, operating pressure, water treatment, and makeup-water quality. Savings also depend upon the quantity of condensate returned to the boiler. With a low percentage of condensate return, more makeup water is required and additional blowdown must occur. Boiler blowdown rates often range from 1% to 8% of the feedwater flow rate, but can be as high as 20% to maintain silica and alkalinity limits when the makeup water has a high solids content. 

### BackgroundTo reduce the levels of suspended and total dissolved solids in a boiler, water is periodically discharged or blown down.High dissolved solids concentrations can lead to foaming and carryover of boiler water into the steam. This could lead to water hammer, which may damage piping, steam traps, or process equipment. Surface blowdown removes dissolved solids that accumulate near the boiler liquid surface, and is often a continuous process.

Suspended and dissolved solids can also form sludge. Sludge must be removed because itreduces the heat-transfer capabilities of the boiler, resulting in poor fuel-to-steam ef ficiency and possible pressure vessel damage. Sludge is removed by mud or bottom blowdown.



### Recommended Practices The American Society of Mechanical Engineers (ASME) has developed a consensus on operating practices for boiler blowdown. Sections VI and VII of the ASME Boiler and Pressure Vessel Code describe recommended practices. The ASME Boiler and Pressure Vessel Code can be ordered through the ASME website: www.asme.org



### 95 A Sourcebook for Industry 

### Appendix B: Steam Tip Sheet Number 23◆ 

### Price and Performance Example For a 100,000 pound-per-hour steam boiler, decreasing the required blowdown rate from 8% to 6% of the feedwater flow rate will reduce makeup water requirements by approximately 2,300 pounds per hour (See Steam Tip Sheet #9, Minimize Boiler Blowdown). Annual energy, water, and chemicals savings due to blowdown rate reductions for a sample system are summarized in Table 1. In many cases, these savings can provide a 1- to 3-year simple payback on the investment in an automatic blowdown control system.

Purchasing and installing an automatic blowdown-control system can cost from $2,500 to $6,000. The complete system consists of a low- or high-pressure conductivity probe, temperature compensation and signal conditioning equipment, and a blowdown-modulating valve. Some systems are designed to monitor both feedwater and blowdown conductivity from multiple boilers. Continuous conductivity recording capability might also be desired. The total cost of the automatic blowdown system is dependent upon the system operating pressure and the design and performance options specified.



### 96 Improving Steam System Performance 

### Appendix B: Steam Tip Sheet Number 23 (continued)

Steam Tip Sheet information is reviewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-102004-1711 • April 2004 • Steam Tip Sheet #23 Blowdown Reduction Annual Dollar Savings ($) (pounds/hour) Fuel Water and Chemicals Total 1,000 $14,925 $4,200 $19,125 2,000 $29,850 $8,400 $38,250 4,000 $59,695 $16,800 $76,495 Savings Through Installation of Automatic Blowdown-Control System

Note: Based on continuous operation of a 150-psig, natural gas-fired steam boiler with fuel valued at $4.50 per million British thermal units, a makeup water temperature of 60°F, and a boiler efficiency of 82%. Water, sewage, and chemical treatment costs are estimated at $0.004 per gallon.

◆ 

### Suggested Actions ◆ • Review your blowdown and makeup water treatment practices; compare them with American Society of Mechanical Engineers

(ASME) practices. • If a continuous-blowdown system is in place, determine the savings an automatic blowdown-control system could attain. Install

conductivity monitoring and automatic blowdown control equipment if the proposed project meets your cost-effectiveness criteria

. • Determine the energy savings and cost-effectiveness from using a heat exchanger to recover energy from the blowdown and

preheat boiler makeup water. Blowdown heat-recovery systems may be economical for boilers with blowdown rates as low as 500 pounds/hour.

# Upgrade Boilers with Energy-Efficient Burners

◆ 

### Background The purpose of the burner is to mix molecules of fuel with molecules of air. A boiler will run only as well as the burner performs. A poorly designed boiler with an efficient burner may perform better than a well designed boiler with a poorburner. Burners are designed to maximize combustion efficiency while minimizing the release of emissions.

A power burner mechanically mixes fuel and combustion air and injects the mixture into the combustion chamber. All power burners essentially providecomplete combustion while maintaining flame stabilization over a range of firing rates. Different burners, however, require different amounts of excess air and have different turndown ratios. The turndown ratio is the maximum inlet fuel or firing rate divided by the minimum firing rate.

An efficient natural gas burner requires only 2% to 3% excess oxygen, or 10% to 15% excess air in the flue gas, to burn fuel without forming excessive carbon monoxide. Most gas burners exhibit turndown ratios of 10:1 or 12:1 with little or no loss in combustion efficiency. Some burners offer turndowns of 20:1 on oil and up to 35:1 on gas. A higher turndown ratio reduces burner starts, provides better load control, saves wear-and-tear on the burner, reduces refractory wear, reduces purge-air requirements, and provides fuel savings.

◆ 

### Efficient Burner Technologies An efficient burner provides the proper air-to-fuel mixture throughout the full range of firing rates, without constant adjustment. Many burners with complex linkage designs do not hold their air-to-fuel settings over time. Often, they are adjusted to provide high excess air levels to compensate for inconsistencies in the burner performance.

An alternative to complex linkage designs, modern burners are increasinglyusing servomotors with parallel positioning to independently control the quantities of fuel and air delivered to the burner head. Controls without linkage allow for easy tune-ups and minor adjustments, while eliminating hysteresis, or lack ofretraceability, and provide accurate point-to-point control. These controls provide consistent performance and repeatability as the burner adjusts to different firing rates.

Alternatives to electronic controls are burners with a single drive or jackshaft.Avoid purchasing standard burners that make use of linkages to provide singlepoint or proportional control. Linkage joints wear and rod-set screws can loosen, allowing slippage, the provision of sub-optimal air-to-fuel ratios, and efficiency declines.

◆ 

### Applications Consider purchasing a new energy-efficient burner if your existing burner is cycling on and off rapidly. Rotary-cup oil burners that have been converted to natural gas use are often inefficient. Determining the potential energy saved by replacing your existing burner with an energy-efficient burner requires several steps. First, complete recommended burner-maintenance requirements and tune your boiler. Conduct combustion efficiency tests at full- and part-load firing rates. Then, compare the measured efficiency values with the performance of the new burner. Most manufacturers will provide guaranteed excess O 2, CO, and NOx levels. 

### Maintenance Requirements
Conduct burner maintenance at regular intervals. Wear on the firing head, diffuser, or igniter can result in air leakage or failure of the boiler to start. One burner distributor recommends maintenance four times per year, with the change of seasons. A change in weather results in a change in combustion.



### Fan Selection Fan selection is also important. Backward-curved fans provide more reliable air control thanforward-curved fans. Radialdamper designs tend to provide more repeatable air control atlower firing rates than bladetype damper assemblies.



### 97 A Sourcebook for Industry 

### Appendix B: Steam Tip Sheet Number 24

### 98 Improving Steam System Performance 

### Appendix B: Steam Tip Sheet Number 24 (continued)

Steam Tip Sheet information is adapted from material provided by PBBS Equipment Corporation and Blesi-Evans Company, and is revi ewed by the DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3463.
DOE/GO-10204-1708 • April 2004 • Steam Tip Sheet #24 ◆ 

### Example Even a small improvement in burner efficiency can provide significant savings. Consider a 50,000 pound per hour process boiler with a combustion efficiency of 79% (E1). The boiler annually consumes 500,000 million British thermal units (MMBtu) of natural gas. At a price of $4.50/MMBtu, the annual fuel cost is $2.25 million. What are the savings from installing an energy efficient burner that improves combustion efficiency by 1%, 2%, or 3%?

Cost Savings = Fuel Consumption x Fuel Price x (1 – E1/E2)

If the installed cost is $50,000 for a new burner that provides an efficiency improvement of 2%, the simple payback on investment is:

Simple Payback = $50,000 ÷ $55,550/year = 0.9 years

◆ 

### Suggested Actions ◆ • Perform burner maintenance and tune your boiler. • Conduct combustion-efficiency tests at full- and part-load conditions.
• If the excess O 2 exceeds 3%, or combustion efficiency values are low, consider modernizing the fuel/air control system to include

solid-state sensors and controls without linkage. Also consider installing improved process controls, an oxygen trim system, or anew energy-efficient burner. • A new energy-efficient burner should also be considered if repair costs become excessive, reliability becomes an issue, energy savings

are guaranteed, and/or utility energy-conservation rebates are available.
• Install a smaller burner on a boiler that is oversized relative to its steam load. Burner Combustion Efficiency Annual Energy Savings, Annual Savings Improvement (%) (MMBtu/year) ($) 1 6,250 $28,125 2 12,345 $55,550 3 18,290 $82,305 Energy Savings Due to Installation of an Energy-Efficient Burner

### 99 A Sourcebook for Industry 

### Appendix B: Steam Tip Sheet Number 25 

# Consider Installing Turbulators on Two- and Three-Pass Firetube Boilers

In a firetube boiler, hot combustion gases pass through long, small-diameter tubes, where heat is transferred to water through the tube walls. Firetube boilers are categorized by their number of “passes,” or the number of times that the hot combustion gases travel across the boiler heat-exchange surfaces. For example, a two-pass boiler provides two opportunities for hot gases to transfer heat to the boiler water. Hot combustion gases enter the tubes in a turbulent flow regime, but within a few feet, laminar flow begins and a boundary layer of cooler gas forms along the tube walls. This layer serves as a barrier, retarding heat transfer.

Turbulators, which consist of small baffles, angular metal strips, spiral blades, or coiled wire, are inserted into the boiler tubes to break up the laminar boundarylayer. This increases the turbulence of the hot combustion gases, and the convective heat transfer to the tube surface. The result is improved boiler efficiency. Turbulators are usually installed on the last boiler pass.

Turbulator installers can also balance gas flow through the tubes by installinglonger turbulators in the uppermost tubes. This practice increases the effectiveness of the available heat-transfer surface by eliminating thermal stratification and balancing the gas flow through the firetubes.

◆ 

### Applications Turbulators can be a cost-effective way to reduce the stack temperature and increase the fuel-to-steam efficiency of single-pass horizontal return tubular (HRT) brick-set boilers and older two- and three-pass oil and natural-gas-fueledfiretube boilers. Turbulators are not recommended for four-pass boilers or coalfired units. A four-pass unit provides four opportunities for heat transfer. It has more heat exchange surface area, a lower stack temperature, higher fuel-to-steam efficiency, and lower annual fuel costs than a two- or three-pass boiler operatingunder identical conditions. New firetube boilers perform better than older twoand three-pass designs.

Turbulators can also be installed to compensate for efficiency losses when a fourpass boiler is being converted to a two-pass boiler because of door warpage and loose and leaking tubes.

Turbulators are a substitute for a more costly economizer or air-preheater. They are simple, easy to install, and low cost. Their installed cost is about $10 to $15 per boiler tube. Current turbulator designs do not cause significant increase in pressure drops or contribute to soot formation in natural-gas-fired boilers. Turbulators are held in place with a spring lock and are easily removed to allow for tube brushing.

Turbulators come in various lengths and widths and should be installed by a qualified installer. To avoid combustion problems, the boiler burner should be retuned after the turbulators have been installed. The installer must also verify that the stack temperature does not fall below the flue gas dew point.

◆ 

### Price and Performance Example A manufacturing facility installed 150 turbulators into their firetube boiler. Tests, conducted both before and after turbulator installation, indicated a reduction in 

### Firetube Boilers The packaged firetube boiler is the most common boiler design used to provide heating or process steam in industrialand heavy commercial applications. The American Boiler Manufacturers Association (ABMA) surveyed high-pressure (15 to 350-psig) firetube and small watertube boiler sales between 1978-1994. ABMA found that firetube boilers comprised over 85% of the sales of these boilers to industry.

Although firetube boilers are available in ratings up to 85,000 pounds of steam per hour, they are generally specified when the required steam pressure is under 150 psig and the boiler capacity is less than 25,000 pounds per hour. Watertube boilersare designed for larger, highpressure, and superheated steam applications.Steam Tip Sheet information is adapted from material provided by Brock Turbulators and Fuel Efficiency, LLC, and is reviewed by t he DOE BestPractices Steam Technical Subcommittee. For additional information on industrial steam system efficiency, contact the EERE Information Center at 877-337-3 463.
DOE/GO-102004-1709 • April 2004 • Steam Tip Sheet #25 the stack gas temperature of 130°F. More combustion heat was being transferred into the boiler water. Because each 40°F reduction in the boiler flue gas temperature results in a 1% boiler-efficiency improvement, overall boiler efficiency is improved by about 3.25%. Fuel costs decrease by approximately 4%.

◆ 

### Example Consider a two-pass firetube boiler that consumes 60,000 million British thermal units (MMBtu) of natural gas annually, and that produces 15,000 pounds per hour of 100 pounds per square inch gauge (psig) saturated steam. What are the annual energy and cost savings, given that the installation of turbulators improves the boiler efficiency from 79% (E1) to 82% (E2)? Natural gas is priced at $4.50/MMBtu.

Energy Savings = Annual Fuel Consumption (MMBtu) x (1 – E1 ÷ E2) or 60,000 MMBtu x ( 1 - 79 ÷ 82) = 2,195 MMBtu/year

Annual Cost Savings = $4.50/MMBtu x 2,195 MMBtu/year = $9,878

If the boiler has 250 tubes and the installed cost for the turbulator is $15 per tube, the simple payback on the investment in the energy efficiency measure is:

Simple Payback = (250 tubes x $15/tube) ÷ $9,878/year = 0.38 years

◆ 

### Suggested Action ◆ Consider installing turbulators in your two- or three-pass firetube boiler tubes if your stack gas temperature is 100°F or moreabove your steam or hot water temperature.



### 100

### Appendix C: Guidelines for Comment

A Sourcebook for Industry 

### 101 

# Appendix C: Guidelines for Comment

Comments that can correct and improve this Sourcebook are appreciated. Please photocopy this page and provide suggestions to the address listed below.

Improving Steam System Performance, A Sourcebook for Industry Comment Form Page Number(s)

Comments

From:

Contact: EERE Information Center P.O. Box 43165 Olympia, WA 98504-3165 www.eere.energy.gov/informationcenter/ Phone: 877-EERE-INF (877-337-3463) Fax: 360-236-2023

### 102 Improving Steam System PerformanceA Sourcebook for IndustryA Strong Energy Portfolio for a Strong America Energy efficiency and clean, renewable energy will mean a stronger economy, a cleaner environment, and greater energy independence for America. Working with a wide array of state, community, industry, and university partners, the U.S. Department of Energy's Offi ce of Energy Efficiency and Renewable Energy invests in a diverse portfolio of energy technologies.



### Industrial Technologies Program U.S. Department of Energy Energy Efficiency and Renewable Energy Washington, D.C. 20585-0121



### Improving Steam System Performance: A Sourcebook for industry One in a series of industrial energy efficiency sourcebooks

To order additional copies of this sourcebook, please contact: EERE Information Center 1-877-EERE-INF (1-877-337-3463) www.eere.energy.gov



### Co-sponsored by:

Council of Industrial Boiler Operators 6035 Burke Centre Parkway, Suite 360 Burke, VA 22015

National Insulation Association 99 Canal Center Plaza, Suite 222 Alexandria, VA 22314

North American Insulation Manufacturers Association 44 Canal Center Plaza, Suite 310 Alexandria, VA 22314

American Boiler Manufacturers Association 4001 North 9th Street, Suite 226 Arlington, VA 22203-1900 

### About the Office of Energy Efficiency and Renewable Energy

DOE/GO-102004-1868 October 2004 Council of Industrial Boiler Owners