A Literature Review of 

the Effects of Smoke 

from a Fire on Electrical 

Equipment 

Office of Nuclear Regulatory Research 

NUREG/CR-7123 
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(NUREG–0750).
A Literature Review of 

the Effects of Smoke 

from a Fire on Electrical 

Equipment 

Manuscript Completed: November 2011 

Date Published: July 2012 

Prepared by: 

Richard D. Peacock, Thomas G. Cleary, Paul A. Reneke, Daniel C. Murphy 

Engineering Laboratory 

National Institute of Standards and Technology 

Gaithersburg, Maryland 20899 

David Stroup, NRC Project Manager 

Prepared for: 

Division of Risk Analysis 

Office of Nuclear Regulatory Research 

U.S. Nuclear Regulatory Commission 

Washington, DC 20555-0001

Office of Nuclear Regulatory Research 

NUREG/CR-7123 

iii

ABSTRACT 

A review is presented of the state of the art of smoke production measurement, prediction of 

smoke impact as part of computer-based fire modeling, and measurement and prediction of the 

impact of smoke through deposition of soot on and corrosion of electrical equipment. The 

literature review on smoke corrosivity testing and damage due to smoke deposition emphasizes 

(despite extensive research on smoke corrosivity) the lack of validated and widely applicable 

prescriptive or performance based methods to assure electrical equipment survivability given 

exposure to smoke from a fire. Circuit bridging via current leakage through deposited smoke 

was identified as a potentially important mechanism of electronic and electrical equipment 

failure during nuclear power plant fires. 

In the near term, assessment of potential damage can reasonably be based on the airborne smoke 

exposure concentration and the exposure duration. Hence, models that can predict the airborne 

smoke concentration would be sufficient to provide upper limit estimates of potential damage. 

In the longer term, it would be desirable to develop models that could estimate the deposition 

behavior of smoke, and specifically correlate the combination of deposited and airborne smoke 

to component damage. 

 

v

CONTENTS 

Section Page 

ABSTRACT ............................................................................................................ iii

CONTENTS .............................................................................................................. v

LIST OF FIGURES .............................................................................................. vii

LIST OF TABLES ................................................................................................ vii

ACKNOWLEDGEMENTS .................................................................................. ix

ABBREVIATIONS AND ACRONYMS .............................................................. xi

1 BACKGROUND ................................................................................................ 1

1.1 Introduction and Purpose ................................................................................................. 1

1.2 Organization of the Report ............................................................................................... 2

2 EFFECTS OF SMOKE ON ELECTRONIC EQUIPMENT ........................ 3

2.1 Nuclear Power Plant Equipment ...................................................................................... 3

2.1.1 Susceptible Components in NPP Applications ......................................................... 3

2.1.2 Equipment Exposure to Full-Scale Fire Environments ............................................ 5

2.1.3 Smoke Exposure Testing .......................................................................................... 6

2.1.4 Early Digital Equipment Testing for NPP Applications ........................................... 7

2.1.5 Smoke Exposure and Circuit Bridging in Digital Equipment .................................. 8

2.1.6 Effects on Smoke on Functional Circuits ............................................................... 11

2.1.7 Other Smoke Effects Testing .................................................................................. 15

2.1.7.1 Conformal Coatings ......................................................................................... 15

2.1.7.2 Digital Throughput .......................................................................................... 16

2.1.7.3 Memory Chips ................................................................................................. 16

2.1.7.4 Hard Disk Drives ............................................................................................. 17

2.1.7.5 Electrical Measurements .................................................................................. 17

2.2 Telecommunications Equipment .................................................................................... 18

2.2.1 Corrosion................................................................................................................. 18

2.2.2 Comparison of Fire Performance and Corrosion .................................................... 20

2.3 Damage Criteria for Electronic Equipment .................................................................... 23

3 MEASUREMENT OF SMOKE PRODUCTION ........................................ 25

3.1 Smoke Opacity Testing .................................................................................................. 25

3.2 Corrosion Test Methods ................................................................................................. 30

3.2.1 Indirect Methods ..................................................................................................... 31

3.2.1.1 Tests for Halogenated Gases: IEC 60754-1 and EN 50267-2-1 ...................... 31

3.2.1.2 Tests for pH and Conductance: IEC 60754-2, EN 50267-2-2 and 

EN 50267-2-3 .................................................................................................. 32

3.2.2 Direct Methods........................................................................................................ 33

3.2.2.1 Static Methods ................................................................................................. 33

3.2.2.2 Dynamic Methods ............................................................................................ 35

3.2.3 Analysis of Individual Standards and Test Methods .............................................. 37
vi

3.2.4 Comparison of Test Methods .................................................................................. 44

4 MODELING OF SMOKE GENERATION, TRANSPORT, AND 

DEPOSITION .................................................................................................. 51

4.1 Use of Smoke and Species Yields as Model Inputs ....................................................... 51

4.2 Smoke and Species Transport ........................................................................................ 52

4.3 Modeling of Deposition on Compartment Surfaces ....................................................... 52

4.4 Modeling of Equipment Damage ................................................................................... 52

5 FUTURE RESEARCH NEEDS ..................................................................... 55

5.1 Smoke Production and Transport ................................................................................... 55

5.2 Modeling Smoke Deposition .......................................................................................... 56

5.3 Prediction of Equipment Damage .................................................................................. 56

6 CONCLUSIONS .............................................................................................. 59

7 REFERENCES ................................................................................................. 61

APPENDIX A MATERIALS INCLUDED IN THE PFPC STUDY ........... A-1 

APPENDIX B EFFECT OF CORROSION PROBE THICKNESS ............ B-1 

APPENDIX C ANALYSIS OF GAS COLLECTION IN A CORROSION 

TEST APPARATUS ............................................................... C-1 

APPENDIX D CONDUCTIVITY AND CORROSION ............................... D-1 
vii

LIST OF FIGURES 

Figure Page 

Figure 1. Functional block diagram of an experimental digital safety channel for NPP 

applications used to evaluate smoke effects on digital equipment [17]. ..................... 7

Figure 2. Change in resistance for 160 Vdc comb pattern circuit boards exposed to smoke from 

a fire source. Data from reference [6]. ....................................................................... 10

Figure 3. HCl yields relative to HCl concentration for several samples of burning PVC cable 

insulation materials. Data from reference [20]. ......................................................... 19

Figure 4. Test results from fire and corrosivity testing of seven commercially-available LAN 

cables. Data taken from [25]. ..................................................................................... 22

Figure 5. The smoke density chamber, ASTM E 662. .............................................................. 26

Figure 6. The ISO 5659 smoke density chamber with inset showing conical radiant heater. .. 27

Figure 7. The OSU calorimeter test, ASTM E 906. .................................................................. 29

Figure 8. The cone calorimeter, ASTM E 1354. ....................................................................... 29

Figure 9. Comparison of corrosion on plain and stainless steel plates after exposure to fire 

smoke. Mass loss typically determined by conductive wire resistance change over 

time [80]. .................................................................................................................... 38

Figure 10. Observed repeatability for a material tested in the cone corrosimeter [77]. .............. 41

Figure 11. Comparison of test results in the cone corrosimeter at 25 kW/m2 and 50 kW/m2 for 

one material. Data from reference [77]. ..................................................................... 42

Figure 12. Comparison of CNET test results with measurements of conductivity for five 

samples tested. Data from references [72,94]. .......................................................... 46

Figure 13. Maximum sample size for given oxygen fuel ratio assuming complete combustion. 48

LIST OF TABLES 

Table Page 

Table 1. Relative ranking of NPP electrical components considering both importance and 

susceptibility to fire damage. Bolded items are ones that were specifically 

mentioned as being susceptible to moisture, particulates, or corrosion. Data from 

reference [14]. .............................................................................................................. 4

Table 2. Soot deposition during smoke exposure tests of functional circuit boards for NPP 

applications. Data from reference [18]. ..................................................................... 13

Table 3. Concentration of chloride, bromide, and fluoride ions during smoke exposure tests of 

functional circuit boards for NPP applications. Data from reference [18]. ............... 13

Table 4. Change in resistance from smoke exposure of an interdigitated comb circuit board 

exposed to fire smoke. Data from reference [18]. ..................................................... 14

Table 5. Conformal coatings applied to functional circuit boards to mitigate the effects of 

exposure to fire smoke. Data from reference [19]. .................................................... 15

Table 6. Results of memory chips exposed to fire smoke. Data from reference [19]. ............ 17

Table 7. Correlation coefficients comparing test results from selected tests of LAN cables. 

Data from reference [25]. .......................................................................................... 21

Table 8. Repeatability of several corrosion standards. Data from reference [79]. .................. 49

ix

ACKNOWLEDGEMENTS 

The work described in this report was supported by the Office of Nuclear Regulatory Research 

(RES) of the US Nuclear Regulatory Commission (USNRC). The project was directed by David 

Stroup of the Fire Research Branch (FRB), Division of Risk Analysis (DRA) in RES. 

 

xi

ABBREVIATIONS AND ACRONYMS 

C Carbon 

CFAST Consolidated Model of Fire Growth and Smoke Transport 

CMOS Complimentary Metal-oxide Semiconductor 

CNET Centre National d'Études des Télécommunications 

CO2 Carbon Dioxide 

DB-9 D-subminiature, 9-pin 

DB-25 D-subminiature, 25-pin 

DIP Dual Inline Package 

DTC Digital Trip Computer 

EDSC Experimental Digital Safety Channel 

EQ Environmental Qualification 

EPRI Electric Power Research Institute 

EPROM Erasable Programmable Read-only Memory 

EVA Ethylene-vinyl Acetate 

FDDI Fiber Distributed Data Interchange 

FDS Fire Dynamics Simulator 

FHA Fire Hazards Analysis 

FMRC Factory Mutual Research Corporation 

FOM Fiber-optic Module 

FR-6400 Low Density Polyethylene with Fire Retardant 

FR-EVA Fire-retardant Ethylene-vinyl Acetate 

HOSTP Host Processor 

HCl Hydrogen Chloride 

HCLV High-current Low-voltage 

HDD Hard Disk Drive 

HF Hydrogen Fluoride 

HFLPF High-frequency Low-pass Filter 

HFTL High-frequency Transmission 

HRR Heat Release Rate 

HSD High-speed Digital 

HVLC High-voltage Low-current 

IEC International Electrochemical Commission 

LAN Local Area Network 

LDPE Low Density Polyethylene 

MCC Motor Control Center 

MLR Mass Loss Rate 

NEC National Electrical Code 

NFPA National Fire Protection Association 

NIST National Institute of Standards and Technology 

NO2 Nitrogen Dioxide 

NPP Nuclear Power Plant 

NRC Nuclear Regulatory Commission 

OSU Ohio State University 

PCB Printed Circuit Board 
xii

PE Polyethylene 

PE165 Polyethylene with Fire Retardant 

PFPC Polyolefins Fire Performance Council 

PLLC Plastic Leadless Chip Carrier 

PRA Probabilistic Risk Assessment 

PRS/MUX Process Multiplexer Unit 

PTH Pin Through Hole 

PVC Poly-vinyl Chloride 

QCM Quartz Crystal Microbalances 

RES NRC Office of Nuclear Regulatory Research 

RH Relative Humidity 

RI/PB Risk-informed, Performance-based 

RJ-45 Network Modular Connector 

SMT Surface Mount Technology 

SNL Sandia National Laboratories 

SO2 Sulfur Dioxide 

SRAM Statis Random Access Memory 

TTL Transtitor-to-transistor Logic 

UL Underwriters Laboratories 
1

1 BACKGROUND 

1.1 Introduction and Purpose 

The Browns Ferry nuclear power plant (NPP) fire in 1975 demonstrated that instrument, control, 

and power cables are susceptible to fire damage [1-3]. At Browns Ferry, over 1,600 cables were 

damaged by the fire and caused short circuits between energized conductors. In addition to the 

cable damage, the fire deposited soot throughout the Unit 1 reactor building and in small areas of 

the Unit 2 reactor building. Examination of all surfaces of piping, conduit, and other equipment 

showed limited evidence of chlorine-induced corrosion, requiring replacement of affected 

material and an accelerated inspection program for some stainless steel within the building [4]. 

In addition to direct damage due to elevated temperature and heat from fires, reports also indicate 

non-thermal damage to equipment that was exposed to smoke and combustion gases from the 

fire environment (see, for example, Refs [23-5]). Although limited information is evident 

specifically related to nuclear power plants [4,6,7], damage to electrical systems in other 

industries from fire has been extensive [5,8], with some resulting in losses in the hundreds of 

millions of dollars [9]. 

Some non-thermal effects occur over long time periods and thus would largely impact clean-up 

and restoration after a fire incident. For example, corrosion several days after a one hour fire 

exposure can be several times that initially observed after the exposure [10]. However, shorterterm effects have also been documented in major electronics fires. In the Hinsdale Illinois 

telecommunications central office fire, smoke-induced failures were noted within six hours [5]. 

Over the past decade, there has been a considerable movement in the nuclear power industry to 

transition from prescriptive rules and practices toward the use of risk information to supplement 

decision-making. One element crucial in supporting the use of risk-informed applications is the 

availability of tools to evaluate the likelihood and consequences of fire scenarios. Riskinformed, performance-based (RI/PB) fire protection often relies on fire modeling to determine 

the consequences of fires. Estimating target damage is a key part of any fire modeling analysis. 

Methodologies are available to obtain reasonable quantitative predictions of thermal damage. 

However, the current state of knowledge does not support similar detailed quantitative prediction 

of smoke damage. 

Based on previous Nuclear Regulatory Commission (NRC) testing [11], four modes of failure 

due to smoke damage have been identified. Of these four failure modes, only one, circuit 

bridging, has been found to be potentially risk significant. Current fire models and data are 

insufficient at this time to directly assess the risk contribution of circuit bridging faults. 

Screening or bounding assessments can be made, but given current knowledge, would be 

dependent on the application of expert judgment and would have considerable uncertainty. For 

example NUREG/CR-6850, “Fire PRA Methodology for Nuclear Power Facilities” [11], 

includes the following recommendations related to smoke damage of electrical equipment: 

 “If the fire scenario involves an electrical panel, it may be prudent to assume the smokeinduced failure of all digital or integrated circuit components within the originating fire 

panel regardless of the assumed fire size, intensity, or duration. 
2

 In the event of a fire involving high-energy electrical components (e.g., MCC, breaker, 

switchgear, etc.), it may be prudent to assume the smoke-induced failure of components 

in adjoining panels or cubicles, especially if those cubicles or panels are connected by 

features like bus ducts or a common ventilation system.” 

Such broad assumed failures have the potential to over- or under-estimate the hazard depending 

on the size and spread of fire and the susceptibility of the equipment to fire. 

In order to assess the potential for damage due to smoke exposure, relationships between smoke 

exposure and the failure of real electronic components need to be established. A smoke damage 

routine developed for a fire model could then assess the near term (during and soon after 

exposure) damage potential of electronics and electrical components design fire exposures. 

1.2 Organization of the Report 

The overall objective of this research program is to develop a better understanding of how fireinduced smoke production and transport can affect electronic equipment that may be used in an 

NPP. This report presents a review of the measurement of the impact of smoke through 

deposition of soot on and corrosion of electrical equipment, smoke production measurement, and 

prediction of smoke impact as part of computer-based fire modeling. 

Chapter 2 presents previous testing of the effects of fire-generated smoke on electronic 

equipment. Studies focused on NPPs and on telecommunication equipment are reviewed. A 

general overview of corrosion of materials exposed to smoke and of existing damage criteria that 

have been applied are included. 

Chapter 3 discusses bench- and large-scale testing and test methods that have been used to 

quantify the production of smoke and its components from a fire. 

Chapter 4 provides an assessment of the state of the art in modeling the generation, transport, and 

deposition of smoke and fire gases in current compartment fire models. 

Chapter 5 identifies future research needs to improve the prediction of smoke transport and its 

potential impact on NPP equipment. 
3

2 EFFECTS OF SMOKE ON ELECTRONIC EQUIPMENT 

In the United States, flammability requirements for electrical equipment are most commonly 

specified in the National Electrical Code (NEC) [12]. Specific testing requirements are then 

defined by testing laboratory standards (e.g., Underwriters Laboratories, Canadian Standards 

Association, etc.). Such standards are essentially voluntary until required by a building code, 

regulatory agency, or by the building owner as part of the bid process for construction of a 

facility. Such requirements are included in the specifications of various organizations such as the 

U.S. Nuclear Regulatory Commission (NRC), the Department of Defense, transportation 

authorities, and other large organizations. These specifications include requirements governing 

the allowable ignition, flame spread, and smoke production of materials, along with the design, 

installation, and use of electrical devices and systems. 

In addition to direct regulation of the flammability and smoke generation properties of materials 

and equipment, there is also interest in indirect effects on the operational capabilities of 

personnel and equipment that may be exposed to a fire environment resulting from a fire. In 

NPP applications, operators must be able to perform appropriate safe shutdown operations and 

equipment may be critical to plant monitoring or to safe shutdown procedures so that both the 

direct effects of fire and indirect effects of fire generated smoke are of interest to ensure safe 

plant shutdown. 

Considerable research has been conducted on the direct effects of fire in NPP applications [11]. 

Recent studies have reviewed potential sublethal effects of fire effluent [13]. A review of both 

direct and indirect effects of fire on electrical equipment [7] was also a resource for this report. 

This chapter provides a review of studies of indirect fire effects on electrical equipment 

including studies specific to NPPs plus a significant base of research related to 

telecommunications equipment. 

2.1 Nuclear Power Plant Equipment 

2.1.1 Susceptible Components in NPP Applications 

The earliest treatment of indirect fire damage to nuclear power facilities is a report prepared for 

the NRC by the NUS Corporation in 1985 [14]. The report evaluates the damaging aspects of 

fire environments, the susceptibility of various components to damage and the importance of 

those components to plant safety. Of particular interest was the impact of 

 conditions associated with suppression activities (high humidity or liquid water effects), 

 elevated temperatures below ignition temperatures of typical materials, and 

 corrosion due to products from cable fire or gaseous suppression agents. 

Components were selected for evaluation based on the Fire Hazards Analysis (FHA) reports 

from four NPPs. Those components necessary to achieve and maintain safe-shutdown were 

evaluated based on Environmental Qualification (EQ) test reports and hydrogen burn tests. The 

EQ reports were used to judge resistance to elevated temperatures and high humidity or liquid 

water effects. The hydrogen burn tests and numerical simulations subjected a variety of 
4

electrical and electromechanical components to elevated temperatures, pressures and humidity 

caused by hydrogen fires in confined spaces. The hydrogen burn results indicated functionality 

of specific components and likely causes of failure. 

Based on the sources above and extensive use of engineering judgment, components were 

assigned ratings in a number of distinct categories describing damageability and significance to 

plant operability. These ratings were weighted according to relative importance and combined 

into a single value to describe the overall hazard produced by exposing a given component to 

adverse environmental conditions. The primary result of these experiments is a relative ranking 

of components by both importance and susceptibility to fire damage. This information, shown in 

Table 1, is expressed for each component as a single number ranging from 0 to 1, with higher 

values indicating greater importance and risk of damage. Because the tests used clean burning 

hydrogen, the applicability of these results is limited with respect to smoke damage, but does 

provide guidance for identifying components that are both important to plant operation and 

sensitive to environmental conditions. It is also worth noting that this assessment applies almost 

exclusively to analog technology. 

Table 1. Relative ranking of NPP electrical components considering both importance and 

susceptibility to fire damage. Bolded items are ones that were specifically 

mentioned as being susceptible to moisture, particulates, or corrosion. Data from 

reference [14]. 

Component Rank Component Rank

Recorders 0.79 Cables, non 1E 0.33 

Logic Equipment 0.77 Thermocouples and RTDs 0.33 

Controllers 0.71 Pressure Switches 0.33 

Power Supplies 0.67 Control Transformers 0.29 

Meters 0.61 Motors (open) 0.28 

Solid State Relays 0.60 Power Transformers 0.26 

Electromechanical Relays/Contactors 0.59 Position/Limit Switches 0.26 

Hand Switches/Pushbuttons 0.50 Valve Positioners/Operators 0.25 

Transmitters 0.50 Gauges 0.20 

MCC 0.49 Cables,1E 0.18 

Switchgear 0.49 Terminal Blocks 0.18 

Battery Chargers/Inverters 0.49 Motors (enclosed) 0.17 

Batteries 0.44 Fans 0.05 

Temperature Switches 0.41 Heaters 0.02 

Distribution Panels 0.38 Valves 0.02 

Indicating Lights 0.37 Pumps 0.00 

Solenoid valves 0.34 

 
5

2.1.2 Equipment Exposure to Full-Scale Fire Environments 

In response to reports of significant damage caused by so called “secondary environments” 

created by fires in NPP and other applications, Sandia National Laboratories (SNL) performed a 

number of cabinet burn tests aimed to better understand the safety issues associated with fires in 

NPPs [15]. These environments include elevated temperatures and humidity and the presence of 

particulates and corrosive gases. The primary goal was to determine functionality of components 

when exposed to these environments. Data were also collected to characterize the environments 

to which those components were exposed. In addition to the burn tests, a small number of 

thermal failure and long term corrosion tests were included. 

The components used in the tests were selected to represent the most easily damaged NPP 

electrical components, as identified in Ref. [14]. Some of these were powered during the test 

and subject to active monitoring, while others were unpowered and evaluated for functionality 

after the test was complete. In order to add conservatism and represent a wider variety of 

designs, some components were placed in non-standard orientations or modified (such as by 

removal of protective cases) to increase susceptibility to expected causes of failure. 

Five burn tests were performed, all using unqualified1

 polyvinyl chloride (PVC)-insulated cable 

as the fuel package. Room size and cabinet configuration were varied as was the arrangement of 

components. The fires lasted between 15 minutes and 40 minutes, and exhibited peak heat 

release rates between 185 kW and 995 kW. The fires were allowed to burn completely; no 

suppression was used. 

Component failures and degradation due to the room-scale burn test were as follows: 

 Switches exhibited slight sensitivity to fire exposure. For some, a small number of 

voltage stresses (at most 15 Vac) were required to resume conduction while others had 

only slight increases in contact resistance. Fire size and exposure were seen as the most 

significant factors contributing to degradation. Overall, fire exposure did not impede 

normal operation of the switches tested. 

 Relays (powered and unpowered) showed minor signs of corrosion after testing but did 

not suffer any loss of functionality. 

 Meters did not suffer any loss of functionality. It is noted that these are generally well 

sealed, making them less susceptible to infiltration by products of combustion. 

 Pen-based chart recorders suffered mechanical failure due to particulate deposition. 

There was no indication of electrical failure. 

 Electronic counters did not fail during the burn test, despite significant particulate 

deposition. 

 Some power supply and amplifiers responded adversely to increased temperatures, but 

were not affected by the products of combustion and functioned properly after the test. 

In a secondary test procedure, the smoke-contaminated electronic counters were subjected to 

high humidity while powered. The less contaminated of the two exhibited no loss of 

 

1

 The IEEE-383 [16] standard provides requirements for qualifying electrical cables and field splices for electrical 

service systems used in nuclear power generating stations. The use of non-qualified cable implies that the wiring 

may not meet the standard requirements and should be considered when assessing the test results. 
6

functionality, while the other failed after an unknown amount of time in a 95 % humidity 

environment. It was determined that the presence of particulates and moisture had resulted in 

leakage currents sufficient to blow a fuse in the device. Removal of contaminants from two 

locations restored functionality. 

The most prevalent acid gas released during NPP fires is likely to be Hydrogen Chloride (HCl) 

since it can be released in significant amounts from burning PVC-containing cables. Active 

measurements of chloride ions in exhaust ventilation were significantly below expected values, 

while concentrations in soot deposits were quite high. The theory presented to explain this 

phenomenon is that the majority of chloride ions were absorbed by smoke particulates in the 

time it takes for them to reach the exhaust vents. The exhaust ventilation system included a 

particulate filter upstream of the chloride ion measurement system, thus any ions absorbed by 

soot would not be measured. It is thought that this phenomenon had not been encountered in 

previous work because of the relatively short time scales associated with small scale tests, which 

would not allow a significant amount of ion absorption. 

2.1.3 Smoke Exposure Testing 

Beginning in 1996, SNL performed a large number of smoke exposure experiments for the NRC. 

In order to create the greatest level on consistency and repeatability, all of these tests used a 

single smoke generation and exposure method loosely based on the withdrawn draft ASTM 

International (ASTM) E05.21.70 corrosivity measurement standard2

. In this method, fuel 

samples are exposed to unpiloted ignition by radiant heat (usually at 50 kW/m2

) and the products 

of combustion are trapped in an enclosed volume containing the components to be tested. When 

possible, the original ASTM E05.21.70 chamber, consisting of a single combustion furnace 

supplying a 0.2 m3 (7.1 ft3) enclosure, was used. For components larger than the original 

exposure chamber, a larger, 1 m3 (35.3 ft3) enclosure supplied by four combustion furnaces was 

used. Unlike the draft standard, which specified fuel packages in terms of surface area and 

volume, the fuel loads for these tests were chosen by weight, in order to produce controlled 

masses of smoke per unit volume in the chamber. Humidity and temperature were kept at 75 % 

relative humidity (RH) and 23.9 oC (75 oF) before and after exposure. The exposure period 

lasted for a total of one hour, with the combustion chambers being active for the first 15 minutes. 

The chamber includes an optical transmission measurement system, which uses a constant flow 

of nitrogen to prevent soot deposition onto its optical surfaces. In some tests, this system was 

deactivated out of concern that the dry nitrogen would artificially lower the humidity of the 

chamber. 

The fuel loads used in these tests were mixtures of a variety of cables that had been identified as 

being in use in NPPs. To the extent possible, the weight fraction of each cable variety was 

selected to match frequency of its usage, to create smoke that would generally represent the state 

of the industry. 

The remainder of this section describes testing which used this exposure method. 

 

2 See Section 3.2.2.1.2 for additional details on the test method. 
7

2.1.4 Early Digital Equipment Testing for NPP Applications 

As digital electronic devices continue to supplant their analog predecessors in NPPs, it becomes 

necessary to evaluate the ability of the new equipment to perform required monitoring and safety 

operations while exposed to adverse conditions. A broad study on the impact of environmental 

conditions on digital systems used in NPPs included an evaluation of smoke effects. Researchers 

at Oak Ridge National Laboratory and SNL subjected an Experimental Digital Safety Channel 

(EDSC) to various smoke loads to monitor its functionality [17]. The EDSC is a network of 

computers and communication devices for monitoring and controlling a nuclear reactor. 

Exposure tests were performed on individual components of the EDSC while they were 

functioning and communicating with the EDSC. The behavior of the entire system was 

monitored for possible failure modes during and after exposure. Due to the size of the EDSC 

components, the larger 1 m3

 chamber was used. 

Three components of the EDSC were exposed to smoke (see Figure 1): the Process Multiplexing 

Unit (PRS/MUX), the Digital Trip Computer (DTC) and the fiber-optic serial datalinks to and 

from the DTC, termed a Fiber-Optic Module (FOM). The PRS/MUX served to convert a 

number of distinct analog electrical signals into a single optical digital signal to be transmitted on 

the Fiber Distributed Data Interchange (FDDI) ring. The DTC interprets optical digital system 

measurement information from the PRS/MUX and transmits optical digital trip (reactor 

shutdown) signals to the Host Processor (HOSTP). 

Figure 1. Functional block diagram of an experimental digital safety channel for NPP 

applications used to evaluate smoke effects on digital equipment [17]. 

FOM 
8

Based on previous work, nominal smoke loads of 3 g/m3, 20 g/m3, and 160 g/m3 were used to 

replicate predicted fire conditions. In order to approximate environmental conditions created by 

suppression activities, some tests introduced steam or CO2. The introduction of 34 g of steam 

immediately after the burning of the fuel raised the relative humidity in the chamber to 85 %. 

The limited number of tests and the re-use of equipment make it difficult to draw strong 

conclusions from the results of these tests. No single combination of conditions and equipment 

was tested more than once, nor were all possible conditions tested. It was noted that pieces of 

equipment that had been exposed to smoke were no longer able to function without error in a 

smoke-free environment, despite having been cleaned after each test. As a result it is difficult to 

distinguish between new and existing damage in the second, third and fourth tests of items. 

In most smoke tests (and some baseline tests after initial smoke exposure), a minor 

communication error requiring that the DTC retransmit data to the HOSTP was recorded. The 

exact cause of this error was not conclusively determined, although it was suspected that 

infiltration of particulates into fiber-optic connections or circuit bridging by particulates was to 

blame. 

 

In two tests, the PRS/MUX was exposed to both smoke and high RH. In both cases, the 

previously mentioned DTC retransmission error occurred. In the case of low smoke density 

(3 g/m2

) no other errors manifested. However, during higher smoke density (20 g/m2), the 

voltage signals transmitted by the PRS/MUX deviated from those given to it as inputs. No cause 

for this behavior is stated explicitly, but circuit bridging is implied. 

In one DTC test and in the FOM test, timeout errors between the HOSTP and DTC occurred on 

three datalink channels. In both cases, it appeared that circuit bridging on edge connectors 

caused the failure. In the FOM test, orientation (vertical or horizontal) had no observable impact 

on failure. The FOMs were exposed to three fuel packages (2.43 g, 15.45 g and 46.42 g) in 

succession without venting the chamber or cleaning components. Both failures occurred one 

hour after the 2.43 g burn, and during the 15.45 g burn. 

Tests of CO2 with or without smoke had no effect on the functionality of the circuits, but did 

drastically reduce the temperature of the environment. 

Overall, SNL concluded that important failure mechanisms included both long-term corrosion 

and short-term current leakage or circuit bridging, particularly on the typically uncoated edge 

connections and interfaces. Digital systems not directly exposed to fire were seen to be able to 

maintain functionality for about one hour following exposure. 

2.1.5 Smoke Exposure and Circuit Bridging in Digital Equipment 

SNL conducted tests specifically to assess the likelihood and impact of circuit bridging in digital 

circuits exposed to smoke. Smoke exposure tests were performed on a group of components 

selected to be typical of modern microprocessor electronics at the time [6]. 
9

During the tests, the smoke exposure environments were altered to represent different fire 

scenarios. The size of the fuel package was varied to either 3 g or 100 g, and in some tests the 

standard fuel mixture was modified to include PVC insulated cables. Other prescribed 

deviations from the standard test procedure were applied in various tests. These modifications 

were reduction of the furnace heat flux to 25 kW/m2, reduction of the humidity to 20 % RH, 

application of compressed CO2 as a post burn suppression agent and inclusion of galvanized 

sheet metal among the test components. The use of galvanized metal was prompted by reports 

on corrosion-related phenomena that can result in conductive liquids capable of damaging 

electronics [6]. 

The first variety of test board had a pattern of copper traces forming four interdigitated combs. 

The theory of the test is that deposition of soot and other products of combustion would provide 

a conductive path between the combs and reduce the overall resistance of the pattern. The initial 

resistance between the combs varied between 1x108 Ω and 1x1015 Ω . During the smoke 

exposure, potentials of 0 V, 5 V, 50 V, and 160 V were applied to investigate the hypothesis that 

local electric fields could promote soot deposition. The results show the relative change in 

resistance after exposure. 

The second test board measured resistances between adjacent leads on a variety of printed circuit 

board (PCB) mounted chip packages. These included four surface-mounted components and 

three through-hole-mounted components. The components represented a range of common 

geometries using either plastic or ceramic packaging. The boards were energized to 5 V and 

actively monitored for resistivity changes during smoke exposure. In every test of the chip 

packages and the comb patterns, four test boards were used; one was kept outside of the 

exposure chamber as a reference, one was kept in a computer chassis inside the exposure 

chamber, one was sprayed with a protective acrylic coating and one was completely unprotected. 

In addition to resistance measurements, the test boards, dual in-line package (DIP) optical 

isolator chips and memory chips were tested for functionality. The optical isolators were 

evaluated by measuring their ability to reproduce a supplied square wave signal, the amplitude, 

and the delay of response to inputs. The exact nature of tests performed on the memory chips 

after exposure is not specified, but rather expressed by pass/fail criteria. 

The most fundamental evaluation of circuit bridging in these tests were active resistance 

measurements of PCBs before, during and after fire exposure. 

It was observed that comb patterns held at higher voltages collected more soot than identical 

patterns with low or no voltage applied. Also, when large particles of soot struck the highest 

voltage patterns (160 Vdc) visible sparks were observed. There were no quantified data 

presented on this topic. 
10

(a) Change in resistance from pretest (X) and during test (Y) 

(b) Change in resistance during test (X) and post-test (Y) 

Figure 2. Change in resistance for 160 Vdc comb pattern circuit boards exposed to smoke 

from a fire source. Data from reference [6]. 

Figure 2(a) shows the resistance before and during exposure for the 160 Vdc comb patterns. The 

line indicates no change in resistance so that points below it correspond to a decrease in 

resistance while points above correspond to an increase. Boards exposed to smoke (bare, coated 

Pre-Test Resistance (log10

0 2 4 6 8 10 12 14 16

Resistance During Test (log10

0

2

4

6

8

10

12

14

16

Bare 

Coated

Chassis

Control

Resistance During Test (log10

0 2 4 6 8 10 12 14 16

Post-Test Resistance (log10

0

2

4

6

8

10

12

14

16

Bare

Coated

Chassis

Control
11

and chassis-mounted) generally showed significant drops in resistance. Some sense of the 

consistency of the experiments can be seen in the results for the control boards, which ideally 

would have exhibited constant resistance but, in fact, increased in resistance. These results are 

representative of data from testing as a whole. Similar resistance changes occurred for lower 

voltage combs and for components mounted to the boards. 

Figure 2(b) presents comparable results for resistance during exposure and averaged over the 

first 22 hours following venting of the chamber. These data provide insight into the tendency of 

components to either recover from damage or suffer long term degradation. Components which 

initially maintained a relatively high resistance tended to recover slightly while those that 

showed large resistance losses during exposure continued to suffer damage after venting. 

In order to determine the significance of test parameters, linear models were constructed to 

predict the resistance before, during and after exposure. Individual factors as well as 

combinations of two and three factors were expressed as binary values and assigned coefficients 

by means of a least-squares regression analysis. Since insignificant factors (those having very 

small coefficients) were omitted, the frequency with which a factor or group of factors appears in 

these models is a strong indicator of the impact (either positive or negative) that it has on circuit 

bridging. The condition of the board (bare, coated or chassis mounted) and humidity level were 

seen to be the most influential individual factors. It is also clear that bare boards were very 

susceptible to a combination of high fuel load and high humidity; while chassis mounted boards 

were heavily influenced by the combination of high fuel load and the presence of galvanized 

metal in the test chamber. Although the presence of PVC in the fuel did not appear to be 

significant, the authors note that the basic cable did contain high concentrations of Cl and Br and 

may have had a similar impact on conductivity and corrosivity of gases. 

In 4 of the 27 tests, the isolator stopped transmitting a signal entirely. In other tests, there were 

significant differences between input and output signals, which could adversely affect the 

function of systems that depend on those signals. The memory chips failed in 6 of the 27 tests. 

In all but one case, failures of these components occurred only when the previously discussed 

linear models predicted low resistance across the leads of DIPs. 

These tests clearly demonstrate the potential of smoke deposition to cause failure of electronic 

systems by circuit bridging. The humidity and amount of fuel consumed both strongly 

contributed to the degree of bridging. Also, flaming rather than smoldering combustion was 

more likely to result in lowered resistance. Conformal coatings and mechanical enclosures were 

seen to provide a measure of protection from smoke. 

2.1.6 Effects on Smoke on Functional Circuits 

SNL also tested complete and functional circuit boards for their susceptibility to damage from 

smoke [18]. These boards contained five functional circuits that could be energized and 

monitored during smoke exposure. Each circuit was present twice on each board, built with 

either surface-mount technology (SMT) or pin through hole (PTH) components. Half of the 

boards tested were protected with a polyurethane conformal coating. The circuits included the 

following: 
12

 High-Voltage Low-Current (HVLC): This high-resistance series of capacitor-resistor 

pairs was subject to a 300 Vdc bias. The nominal current was 6 μA. Within the network 

itself, the potential difference between any two adjacent copper traces was 60 Vdc. 

 High-Current Low-Voltage (HCLV): This circuit contained a number of resistors and 

capacitors in parallel. A constant-current power supply adjusted the applied voltage to 

maintain 1 A through the nominal 1.43 Ω. 

 High-Speed Digital (HSD): This circuit simply connected a series of NAND logic gates. 

While powered, a 5 V, 20 ns input pulse was applied to the first gate, and the output of 

the final gate was monitored. Increases in the rise, fall and delay (relative to input) times 

of the output square pulse all indicate degradation of a circuit. 

 High-Frequency Low-Pass Filter (HFLPF): a system of inductors and capacitors 

configured to attenuate high frequency input signals. Before and after exposure, the 

filters were tested for signal attenuation from 50 MHz to 1 GHz. During exposure, they 

were tested for: attenuation at 50 MHz, 250 MHz and the frequencies at which 

attenuation reached -3 and -40 dB. 

 High-Frequency Transmission Line (HFTL): this circuit was two adjacent PCB copper 

traces, designed to exhibit 50 Ω impedance. It is expected that a small amount of a signal 

on one line will be transmitted to the other. This behavior, referred to as coupling, is 

frequency dependent and is expected to increase with the conductivity between the lines. 

During exposure, coupling between the lines was measured at 50 MHz, 500 MHz and 1 

GHz. Pre- and post-exposure tests added measurements of coupling with the second line 

connected in a reversed configuration. 

In addition to the functional circuits, additional components on the board were tested for leakage 

currents before, during and after exposure. Further leakage current measurements were 

performed using an interdigitated comb test board. Each board had four distinct comb patterns 

and during exposure, two were biased with 5 Vdc and the other two with 30 Vdc. 

The tests used the standard exposure method, with fuel loads of 3 g/m3

, 25 g/m3 and 50 g/m3

heated with 50 kW/m2 and 25 kW/m2

. Soot deposition was measured with two quartz crystal 

microbalances (QCM), one oriented vertically and the other oriented horizontally. The quantities 

deposited and fuel burned are listed below in Table 2. Note that the 25 kW/m2

 heat flux 

exposures caused smoldering of the fuel while the 50 kW/m2 flux caused flaming. 
13

Table 2. Soot deposition during smoke exposure tests of functional circuit boards for NPP 

applications. Data from reference [18]. 

Fuel 

level 

(g/m3) 

Fuel 

available 

(g) 

Flux level 

(kW/m2

) 

Fuel 

burned 

(g) 

Vertical 

deposition 

(μg/cm2

) 

Horizontal 

deposition 

(μg/cm2) 

Deposition 

ratio 

(V/H) 

3 6 25 0.27 0.4 2.8 0.14 

3 6 50 0.49 0.9 3.4 0.27 

25 5 25 3.12 2.1 45.3 0.05 

25 5 50 3.95 4.2 17.6 0.24 

50 10 25 6.49 3.2 94.8 0.03 

50 10 50 7.34 7.3 58.5 0.13 

Chemical analysis of soot was performed on deposits collected by 14.2 cm2 disks of ashless filter 

paper on the floor of the test chamber (Table 3). With the larger fuel packages, smoldering 

resulted in larger quantities of deposited chloride and bromide. 

Table 3. Concentration of chloride, bromide, and fluoride ions during smoke exposure 

tests of functional circuit boards for NPP applications. Data from reference [18]. 

Fuel level 

(g/m3

) 

Flux level 

(kW/m2) 

Chloride 

(g/Filter) 

Bromide 

(g/Filter) 

Fluoride 

(g/Filter) 

3 25 95.5 2.1 0.0 

3 50 24 5.5 0.25 

25 25 92.6 96.6 0.0 

25 50 73.0 66.9 1.45 

50 25 147 181 1.25 

50 50 95.4 165 0.0 

Unexposed filter 0 3.9 0.0 0.7 

 

No direct measurements of corrosion were performed, but visual inspection of components 

showed that components made of reactive metals (such as nickel) had corroded significantly 

after the test. 

The HVLC circuit showed susceptibility to smoke exposure. Resistance decreased noticeably 

with smoke density and recovered somewhat after venting of the chamber. Conformal coatings 

were very effective at preventing or limiting resistance losses for all fuel loads. In this particular 

circuit, the PCB traces were the most vulnerable to damage because they carried the highest 

potential differences and were more closely spaced than the leads of attached components. 

Because this vulnerability was independent of the types of components attached, there was no 

observed difference between PTH and SMT. 

The HCLV circuit was largely insensitive to smoke. Because the circuit had a very low initial 

resistance, the addition of weakly conductive alternate paths would have little impact. The 

exception was the case of the bare (having no conformal coating) SMT board. In all of the 

medium and high fuel load tests, the resistance of these circuits increased measurably (0.9 % - 
14

1.7 %) and did not recover after venting. This change is attributed to corrosion of contacts or 

solder joints. None of the changes in these tests represented a significant effect on system 

performance. 

The HSD circuit was tested for its response to a 20 ns, +5 Vdc pulse by measuring the output rise 

time, fall time and delay. Changes in signal degradation due to differences in cable length make 

direct comparison between pre-test results and in situ measurements invalid. However, none of 

the circuits showed significant change in response to changing fuel loads or the presence of 

conformal coatings. Previous work indicates that the highest fuel load used would have caused 

failure due to circuit bridging in complementary metal-oxide semiconductor (CMOS) chips, but 

that advanced Schottky transistor to transistor logic (FAST TTL), such as those in the HSD, are 

less sensitive. 

The HFLPF did not show any response to smoke. However, active measurement during 

exposure was performed with an input frequency (250 MHz) that would not be impacted by 

changes in system capacitance due to debris (the expected failure mode). Post-test 

measurements over a wider range of frequencies showed no change from the pre-test condition. 

It was expected that the most severe changes in capacitance would occur during exposure, when 

the testing method would be unable to measure those changes. 

The HFTL circuit was tested to determine coupling between two adjacent lines. Coated boards 

showed no change in coupling during or after exposure. The bare board experienced a large 

(from -52 dB to -17 dB) increase in coupling of 50 MHz signals during exposure. Coupling on 

the bare board returned to pre-test values quickly after venting of the test chamber. At high 

frequencies (500 MHz and 1 GHz) coupling on the bare board actually decreased during smoke 

exposure and returned to pre-test values after venting. 

Leakage current data are presented only for the PTH boards and the interdigitated comb; leakage 

data for other components in the methodology section were not reported. Resistance on the bare 

boards dropped as fuel load increased and recovered somewhat after venting. Changes in the 

interdigitated comb were less consistent, but surface resistance generally decreased with 

increasing fuel loads and partially recovered after venting. Results in Table 4 are presented in 

the change of Log10(R) between pre-test values and average during smoke exposure. 

Table 4. Change in resistance from smoke exposure of an interdigitated comb circuit 

board exposed to fire smoke. Data from reference [18]. 

Fuel(g) / Flux(kW/m2

) 0/50 3/25 3/50 25/25 25/50 50/25 50/50 

ΔLog10(R) boards 0 0 -1.5 -6.1 -6.3 -6.5 -6.7 

ΔLog10(R) comb (5V) 0.6 0.7 0.3 -0.6 -1.5 -2.6 -1.9 

ΔLog10(R) comb (30V) 1.2 0.1 -1.9 -0.2 -3.2 -1.1 -2.8 
15

2.1.7 Other Smoke Effects Testing 

In a final report in the series of non-thermal damage experiments, SNL reports on previously 

unpublished results including tests of conformal coatings, digital throughput, memory chips, hard 

disk drives, and electrical properties of fire smoke [19]. 

2.1.7.1 Conformal Coatings 

In order to gauge the ability of conformal coatings to mitigate the effects of smoke exposure, a 

battery of high smoke load (200 g/m2

) exposure tests were performed on functional boards with a 

variety of conformal polymer coatings (listed in Table 5, below) [19]. The circuits tested were 

the previously discussed HVLC, HCLV, HSD, HFTL and HFLPF constructed from PTH and 

SMT components. There were variations in response with different coating chemistries and 

electrical components, but in general, coated boards were less susceptible to damage than bare 

boards. 

Table 5. Conformal coatings applied to functional circuit boards to mitigate the effects of 

exposure to fire smoke. Data from reference [19]. 

Coating Type Brand3 Product Thickness 

(mils) 

Application Method 

Acrylic Humiseal 1B-31 2.5 Dipped 

Epoxy Envibar UV1244 2.5 Dipped 

Parylene Union Carbide Type C 0.75 Vacuum Deposited 

Polyurethane Conap CE-1155 2.5 Dipped 

Silicone Dow 3-1765 5 Dipped 

When constructed from PTH components, the HVLC circuit maintained its resistance best with 

parylene or polyurethane coatings and varied the most (excepting the bare board) with the 

silicone coating. The SMT components maintained resistance well with parylene, polyurethane 

and acrylic coatings. Although the expected and most commonly observed degradation mode in 

the HVLC circuit was a loss of resistance, some PTH components showed increases in resistance 

during the burn phase of testing. It should also be noted that the epoxy coated SMT board did 

not recover appreciably after smoke was vented from the chamber, a behavior which was not 

observed in any other configurations (including bare boards). 

In the HCLV tests, only the bare SMT board showed a noticeable change. After the burn began, 

the resistance of the circuit rose from 1.46 Ω to 1.49 Ω. Resistance continued to increase slowly 

until the chamber was vented, at which point it remained constant. The bare SMT board showed 

no signs of recovery. With such a small change in resistance, it is not clear that this is a 

significant result. 

 

3

 Certain commercial entities, equipment, or materials may be identified in this document in order to describe an 

experimental procedure or concept adequately. Such identification is not intended to imply recommendation or 

endorsement by the National Institute of Standards and Technology, nor is it intended to imply that the entities, 

materials, or equipment are necessarily the best available for the purpose. 
16

The HSD was protected very well by all conformal coatings. Of the 18 bare boards (9 SMT and 

9 PTH), 7 PTH boards and one SMT board experienced momentary transmission failures at 

some time after testing. Also, post test measurements showed that fall time response on the bare 

PTH increased from 1.6 ns to 2.2 ns, while SMT and all coated boards remained unchanged. 

As observed in previous tests, the bare transmission line circuits showed increased forward 

coupling at 50 MHz and decreased forward coupling at 500 MHz and 1 GHz while smoke was 

present. Coated boards showed no coupling response to smoke. 

The bare HFLPF circuits were mildly affected by smoke exposure, while coated boards showed 

almost no response. 

2.1.7.2 Digital Throughput 

Smoke exposure tests were performed with a variety of fuels to determine the impact of smoke 

exposure on digital cable connectors [19]. A circuit board with linked pairs of D-subminiature 9-

pin (DB-9), D-subminiature 25-pin (DB-25) and network modular (RJ-45) connectors was 

placed in the exposure chamber. Digital signals from a personal computer outside of the 

chamber were routed through this board in order to determine the impact of smoke upon these 

connectors. PVC, Douglas fir and jet fuel were used as fuels for these tests, rather than the 

standard cable mixture. 

DB-9, DB-25 and RJ-45 connectors were tested simultaneously in 19 tests and showed no signs 

of failure. Subsequent tests performed by intentionally bridging signal lines with a variable 

resistance indicate that conductance between pins on a connector must closely approach the 

conductance of the cables themselves before there is a significant risk of failure. 

2.1.7.3 Memory Chips 

Smoke exposure tests were performed on memory chips to determine functionality and attempt 

to isolate physical parameters that can predict chip failure [19]. The standard exposure method 

and fuel mixture were used, with additional electrical testing continuing for one hour after 

venting the chamber. Smoke loads of 30 g/m3

, 35 g/m3, 50-60 g/m3, and 150 g/m3 were used. 

The five types tested were 3.3 V volatile Static Random-Access Memory (SRAM), 5 V volatile 

SRAM, DIP Erasable Programmable Read-Only Memory (EPROM), plastic-leadless chip carrier 

(PLCC) EPROM and 5V non-volatile SRAM. 

Functional testing of the chip consisted of repeatedly writing data to the chips and reading it 

back. The response time of the chips and the error rate of read/write operations were recorded. 

The parametric measurements monitored leakage current behavior. The current drawn when the 

chip was powered but not operating, current when a standard voltage is applied to a given pin 

and the voltage required to maintain a particular current were measured repeatedly at 30 s 

intervals. 

The exposure tests for electronic memory determined both functionality and the electrical 

parameters (voltage, current etc.) of the chips during and after smoke exposure. Functionality 
17

was determined by the ability of the chip to be accurately written to and read from. Table 6

indicates success and failure rates. The non-volatile SRAM suffered no failures even at higher 

(150 g/m3) fuel loads. 

Table 6. Results of memory chips exposed to fire smoke. Data from reference [19]. 

Fuel Load 30 g/m3

Pass/Tested 

50- 60 g/m3

Pass/Tested 

3.3 V SRAM 2/2 0/4 

5V SRAM 2/2 2/4 

DIP EPROM 1/1 5/5 

PLCC EPROM 1/1 5/5 

Comparison of failures to the parametric data showed no consistent correlation between leakage 

current and failure. When the 3.3 V SRAM chips failed, their operating current roughly doubled, 

while the operating current of the 5 V SRAM dropped to half of normal during failure. Although 

some of the recorded failures occurred shortly after the smoke chamber vented, all chips 

functioned properly when tested several weeks later, indicating recovery after exposure. 

2.1.7.4 Hard Disk Drives 

Hard disk drives (HDD) isolated from other computer components were tested for read/write 

functionality during and after exposure and were scanned for corrupted data sites after exposure 

[19]. Five drives were tested six times. In the first test the drives were oriented as they would be 

in normal use. In all subsequent tests, the drives were inverted to increase soot deposition onto 

exposed circuit boards on the underside of the drives. The standard smoke exposure method was 

used with fuel loads of 15 g and 30 g. In two of the tests, the nitrogen purge protecting the optics 

was deactivated, to prevent the dry nitrogen from lowering the humidity of the chamber. All 

drives passed the in situ functionality tests. One of the 5 disks showed signs of corrupted data, 

but the cause was not identified. 

2.1.7.5 Electrical Measurements 

Two important electrical properties of smoke are conductivity in the gas phase and conductivity 

on surfaces. Surface conductivity measurements were performed with the previously described 

interdigitated comb and a specialized low-mass comb board. Gas conductivity was measured 

with pairs of freestanding, parallel perforated stainless steel plates. Masses of fuel between 1.5 g 

and 19 g were used. 

The comb patterns were biased with 5 V, 50 V and 500 V during exposure. Current flow was 

measured continually during and after exposure. The boards were weighted and visually 

inspected after exposure, to identify the mass and physical distribution of the deposited smoke. 

In one set of tests [19], the vertical plates were placed with a fixed spacing of 2.5 mm. In these 

tests, the plates were biased with 5 Vdc, 50 Vdc, 500 Vdc and 1 Vac. The current flow between 

the dc-biased plates was monitored during exposure. The ac-biased plates were analyzed to 
18

measure admittance from 500 kHz to 30 MHz. Video of these experiments was recorded to 

monitor the behavior of soot particles in electrical fields. 

In a different set of experiments [19], the plates spaced at distances from 3 mm to 25 mm 

subjected to a rising ac bias, up to 4.2 kV. The voltage was allowed to rise until arcing occurred. 

Current and voltage behavior during arcing were measured. 

It was found that higher voltages (50 V and 500 V) attracted smoke particles to the plates and 

significantly increased conductance between the plates. The smoke particles were observed to 

accumulate between the two plates and create conductive bridges. As a result, conductance 

increased very quickly with smoke density but decreased much less quickly and leveled out at 

approximately 20 % of its peak value. Conductance only returned to near zero values when 

forced ventilation of the chamber disrupted the accumulated soot bridges. 

The interdigitated comb boards biased at 5 V, 50 V and 500 V were tested for conductance over 

time and total mass of smoke deposited. Inspection of the boards after exposure showed that 

soot preferentially deposited on the traces of the boards at higher voltages, resulting in a less 

even distribution of soot on the 50 V and 500 V boards. Although distribution pattern varied 

with voltage, the total mass deposited depended only upon the total fuel load. Conductance 

increased sharply with the smoke level and decreased as the smoke cleared. The conductance of 

the 5 V board recovered far less effectively than the 50 V and 500 V boards. It was suggested 

that this was due to the more even distribution of soot. 

2.2 Telecommunications Equipment 

Outside of the nuclear power industry, the overall cost of a fire may be more important than a 

temporary loss of functionality. While the short term failure of equipment has a cost in lost 

business, the damage caused by non-thermal fire environments can easily total millions of dollars 

[3]. Thus, the cost of a fire event can be significantly decreased if components exposed to 

smoke can be recovered and returned to service, rather than being replaced. As such, much of 

the research in this industry has focused on understanding and mitigating the forms of nonthermal damage that can decrease the lifetime of equipment. 

2.2.1 Corrosion 

The most commonly identified and studied mechanism of non-thermal damage is corrosion 

caused by the chemical products of combustion [20 - 23]. Starting in the late eighties, prompted 

by reports of extensive corrosion damage and accumulated corrosive products found in a number 

of separate telecommunications facilities during the 1970’s and 1980’s, researchers began to 

develop the theoretical and empirical basis for characterizing the release, transport and impact of 

corrosive compounds from fires. 

A significant part of this work was the development of a number of bench-scale laboratory 

experimental testing methods for determining the potential of the combustion products of a 

particular fuel to corrode metal (detailed in section 3.2). However, these standards are of a very 

simplistic nature and do not necessarily provide immediate insight into the complex phenomena 
19

associated with real-world fire scenarios. In order to develop prevention and recovery 

procedures, a number of intermediate and full scale test fires of a more realistic nature were 

required. 

The first steps that Tewarson and Chu [20] took in evaluating the non-thermal damage potential 

of cables used the Factory Mutual Research Corporation’s (FMRC) 50 kW-scale flammability 

apparatus to evaluate ignition and flame spread characteristics as well as yields of products. This 

device subjects a vertically oriented sample to radiant heating and a controlled flow of gas at the 

component sample. The composition of the effluent is analyzed to determine chemical 

composition, which is used to determine corrosive properties and heat release rate. The 

separation of chemical product distributions and fire properties allows for a more detailed 

understanding of the factors that contribute to corrosive damage. Figure 3 shows the HCl yields 

(g/g) relative to HCl concentrations (g/m3

) in the effluent stream for a selection of PVC cable 

insulation materials. The weak correlation between the two data sets is a result of the burning 

rate of the fuels and the dynamic nature of this test method. The forced flow ensures a relatively 

constant mass flow of air, while the mass release rate of HCl depends on the burning rate of the 

material. Thus, materials rich in chlorine will produce relatively low concentrations in the gas 

phase if they burn slowly. Further, the flame propagation rates are seen to play a key role in 

determining the amount of fuel that will become involved before intervention occurs in a fire 

Figure 3. HCl yields relative to HCl concentration for several samples of burning 

PVC cable insulation materials. Data from reference [20]. 

Corrosivity

Sample Number

0123456

HCL Yield (g/g)

0.00

0.02

0.04

0.06

0.08

0.10

0.12

HCL concentration (g/m3

)

0.00

0.05

0.10

0.15

0.20

0.25

0.30
20

event. Again, a chlorine rich material may prove to be less of a corrosion hazard than a material 

with only modest chlorine levels if it is less flammable. This illustrates the importance of 

considering the interaction of a complete range of physical behavior when determining the 

meaning of a parameter such as chlorine concentration. 

The prevalence of corrosive compounds in telecommunications fires is often a result of 

halogenated compounds used as solid fire retardants and gaseous suppression agents [24]. 

When fires involving these compounds do occur, significant quantities of the hydrogen halides 

and halogen radicals may be released along with the other products of combustion. Therefore, 

the use of these compounds to reduce the risk of a fire may carry with it the potential to increase 

the severity of non-thermal damage caused by any fire that does develop [24]. 

A commonly identified corrosive reaction is that of hydrogen chloride with zinc. [21,22] This 

has been observed in a number of fires, because of the prevalence of galvanized (zinc coated) 

steel in HVAC systems as well as support structures in electronic equipment. The solid zinc 

chloride adheres well enough to the base metal that it poses little direct hazard to electronics. 

However, the ZnCl2 is extremely hygroscopic, being able to absorb water in relative humidity as 

low as 10 %. The ZnCl2 is very conductive and can easily flow or drip onto nearby electronics, 

causing circuit bridging. 

2.2.2 Comparison of Fire Performance and Corrosion 

Work by Chapin et al. [25] evaluated the ability of a variety of standard test methods to evaluate 

the impact of smoke from local area network (LAN) cables on electrical equipment. Their 

concern was that the specialized and controlled nature of these tests may prevent them from 

realistically predicting corrosion and, more importantly, overall functionality of electronics 

exposed to smoke. They examined correlation among the standard tests and provided a 

discussion of the sensitivities and possible sources of error. 

Although the discussion and findings address a larger number of tests, the authors performed 

experiments with only three previously existing test methods. ASTM test D5485, International 

Standards Organization (ISO) test DIS 11907-3 and International Electrotechnical Commission 

(IEC) test 60754-2 are described in section 3.2 of this report. These tests burn complete 

products, individual conductors, or raw materials (individual components of wire insulation) to 

classify their tendency to cause corrosion. Both the ASTM and ISO tests subject electrically 

conductive copper corrosion probes to the smoke produced. The change in conductivity of these 

copper surfaces is used to estimate the amount of metal lost, and results are expressed as 

thickness consumed (ASTM) or percent consumed (ISO). The IEC test measures pH of gases 

produced in the burning of a material. Note that the IEC test evaluates individual materials, and 

as such, cable coatings must be separated into their jacket and insulation materials for isolated 

testing. 

To complement results from the corrosivity standard, other measurements were made to evaluate 

the fire behavior of the cable samples. The chemical compositions of the cable jacket and 

insulation materials were determined. Each variety of cable was subjected to the ASTM E1354 

cone calorimeter. This uses the same combustion apparatus as the ASTM D5485, but produces 
21

heat and smoke release measurements rather than capturing corrosive gasses. This information is 

used in more traditional analysis of flammability and fire hazards. The smoke release data 

provide interesting context for the corrosivity measurements by allowing one to evaluate the 

likelihood and severity of fires involving those materials. 

The authors report that, in the course of previous work, they have observed that smoke most 

often causes the failure of digital electronic systems by decreasing surface resistivity. In an 

effort to quantify this behavior relative to the corrosivity tests, the authors developed a test 

apparatus to measure changes of surface resistivity of a circuit board exposed to smoke. The 

tube furnace used in the IEC 60754-2 test was fitted with an exposure chamber into which the 

products were driven by forced air flow. The chamber was used to expose printed circuit boards 

with an interdigitated comb pattern (similar to those used by SNL for the circuit bridging tests 

described in Section 2.2). After exposure, the targets were tested for current flow with an 

applied 50 V potential. Leakage currents were tested in a controlled humidity chamber over a 

range of relative humidity from 30 % to 90 %. 

Seven commercially available LAN cables were used in these tests. Three of the varieties were 

rated for plenum use according to Underwriters Laboratories (UL) test 910, indicating a very low 

fire hazard. The other cables were rated for other use under different UL and IEC tests. All of 

the plenum rated cables and some of the non-plenum cables contained large quantities of 

halogens, which are often cited as a major contributing factor in corrosion caused by smoke [20 - 

22]. 

For the purposes of comparison, results have been normalized by the average value from each 

test method, and the pH measurements for the IEC 60754-2 have been inverted such that higher 

values indicate higher acidity. Comparisons of the test results and the correlation between tests 

are shown in Table 7 and Figure 4 calculated as correlations coefficients from the data in 

reference [25]. 

Table 7. Correlation coefficients comparing test results from selected tests of LAN cables. 

Data from reference [25]. 

Total 

Smoke 

ASTM 

D5485 

Jacket pH Insulator 

pH 

ISO DIS 

1197-3 

Leakage 

Total Smoke 1 0.707 0.274 -0.222 0.193 0.802

ASTM D5485 1 0.551 -0.023 0.728 0.377342

Jacket pH 1 0.734 0.519 -0.095

Insulator pH 1 0.297 -0.369

ISO DIS 1197-3 1 -0.056

Leakage 1
22

The plenum-rated cables (cables A,F,I) are easily differentiated from the non-plenum cables by 

the leakage current test. Leakage currents caused by the plenum cables were 3 to 7 orders of 

magnitude lower than the highest performing non-plenum cable (K). It may also be possible to 

make such distinctions based upon smoke load, which was higher for non-plenum cables. The 

correlation between smoke load and leakage current is consistent with the premise that leakage 

currents are the result of circuit bridging by particulates in smoke, as has been found by Chapin 

et al. [25] and Tanaka [18]. 

This low smoke load produced by plenum cables is not surprising, as UL 910, which is based on 

the method developed by Steiner [26], includes criteria for smoke production as well as heat 

release rate (HRR) and flame spread. UL 910 was specifically designed to limit smoke 

Figure 4. Test results from fire and corrosivity testing of seven commercially-available 

LAN cables. Data taken from [25]. 
23

production from cables in a plenum configuration [27]. Products that pass can be expected to 

produce very small amounts of smoke. 

The simple calculation of correlation coefficients could suggest that ASTM D5484 is sensitive to 

smoke load. However, a more careful examination of material composition would indicate that 

the presence of PVC is the more important factor. The three cable products (cables I,G,B) which 

caused significant corrosion in this test all used PVC in their jacket and/or insulation, while the 

other cables did not. It is interesting to note that cable F contained a low smoke PVC-based 

compound but produced negligible corrosion in ASTM D5484. The amount of smoke actually 

produced by this cable was slightly higher than the highly corrosive cable I. As both contained 

similar amounts of chlorine, this suggests that the mechanism used for smoke suppression may 

also serve to decrease the corrosivity of the combustion products. A larger sample size and a 

more detailed treatment of the chemistry involved would be required to develop a full 

understanding of any role that fire retardant compounds may play in corrosion. 

Results of the ISO DIS 11907-3 test are more difficult to explain. The three cables which caused 

corrosion in the ASTM D5484 (cables I,G,B) did so in this test as well. The smoke suppressed 

PVC cable (F), was comparable to one of the ordinary PVC cables (G). Further, the two nonhalogenated cables caused between 25 % to 50 % as much corrosion as the PVC cables in this 

test as opposed to less than 10 % in the ASTM test. Chapin et al. [24] argue that the corrosion 

target used in the ISO test may produce inaccurate results, due to circuit bridging. The target 

tracks material loss in the form of increased resistivity in a closely packet serpentine copper trace 

on a circuit board. They express concern that connections across the board could decrease 

effective resistance, resulting in underestimation of total mass loss. 

The only consistent behavior from the IEC 754-2 pH tests was that halogenated polymers 

produced low pH, while non-halogenated polymers did not. There was no strong correlation to 

either of the direct corrosion tests. 

None of the corrosivity tests correlated well with one another or with the leakage current test. As 

such, it is difficult to draw any specific conclusions as to the quality of particular test. The lack 

of agreement between generally similar tests (such as ASTM and ISO) serves to illustrate the 

need to understand complex nature of corrosion phenomena in order to properly assess the threat 

posed by smoke. While Chapin et al. [24] claim that circuit bridging is the most important factor 

in the failure of electronics, others have presented cases in which corrosion dominated equipment 

losses [20,21]. 

2.3 Damage Criteria for Electronic Equipment 

Early reports on non-thermal damage to telecommunications were based on observations of the 

methods required to recover equipment from fire events. These reports categorize the level of 

damage to equipment based on the acid gas concentration on component surfaces. Both 

Tewarson and Reagor report that deposited mass of chloride can be a predictor of corrosive 

damage. However, the thresholds specified differ [20,21]. Reagor categorizes four levels of 

contamination by mass of chloride deposited per unit area: clean at less than 2 μg/cm2, easily 

cleaned and recovered below 30 μg/cm2

, difficult but possible to recover between 30 μg/cm2 and 
24

90 μg/cm2, and above 90 μg/cm2 it is increasingly likely that the cost of cleaning the component 

will be greater than simply replacing it. Initially, Tewarson specified a minimum concentration 

of 0.98 μg/cm2

 coupled with relative humidity greater than 30 % at 20 °C (68 °F) and gas 

concentrations of 100 ppm HCl or 1000 ppm of NO2, HF, SO2 or acetic acid. In subsequent 

literature, Tewarson cites Reagor’s criteria [28]. 

Tanaka and Tanaka et al. [18,29] studied failure criteria for digital logic circuits exposed to 

smoke. In order to evaluate the loss of functionality of the logic circuits, the loss of resistance 

due to smoke was simulated with a variable shunt circuit to determine the point of failure for a 

range of circuits. Components with a high tolerance to resistance loss are seen to be more 

tolerant to smoke exposure. Critical resistance at failure varied for different chips designs, but 

was highly correlated to the output current of the device. Higher current outputs were seen better 

able to supply the necessary current to maintain a voltage level despite the loss of resistance due 

to the shunt. 
25

3 MEASUREMENT OF SMOKE PRODUCTION 

During the 1940s and the 1950s, flammability (or “reaction-to-fire”) tests were developed on a 

purely ad hoc basis. Results were typically expressed by arbitrary 0 to 100 scales or by such 

rating terms as “self-extinguishing.” In 1973, the U.S. Federal Trade Commission saw such 

practices as misleading and sued a number of plastics manufacturers and also the American 

Society for Testing and Materials (ASTM) [30]. A consent agreement was eventually reached 

whereby a Bunsen burner test, ASTM D 1692, was dropped, and a caveat was inserted into other 

ASTM tests, in an attempt to avoid their future misuse. It is noteworthy that the situation in 

other countries is similar to the U.S. experience. More than thirty years ago, Emmons obtained 

the results of flammability tests on a number of materials, when tested according to various 

national, bench-scale flammability standards [31]. He found that the relationship between the 

test results and real-scale fire behavior according to the different standards was almost 

completely random. In 1987, Östman and Nussbaum re-examined this issue; the situation 

appears to have improved only slightly [32]. The reason is that the new knowledge gained in fire 

physics and engineering over the last decades has generally not yet been reflected in many of the 

required testing standards. 

This is due at least partly to the great number of national test methods that exist for fire testing. 

For example, one such compilation which includes only the ASTM fire test methods [33] 

tabulates some 167 test standards covering a broad range of measurements. Based on this large 

number of tests, it may seem that fire test methods are highly refined and well tuned to specific 

areas. Though many of the currently published methods were developed up to 40 years ago, for 

smoke production and for most other fire test results, the focus has shifted to appropriate input 

data for predictive modeling methods. This chapter provides a review of both types of test 

methods use to quantify smoke production, those that primarily provide a ranking of materials, 

and those that provide quantitative input for modeling calculations. 

3.1 Smoke Opacity Testing 

Typically, bench-scale test methods designed to measure the impact of fire smoke provide a 

measurement of opacity, an indication of visibility through the smoke. The most significant body 

of work in this area has been accomplished by Jin [34–36], who found that there is an 

approximate reciprocal relationship between smoke opacity and visibility distance (the distance 

at which a person can identify an exit sign, for example), according to 

kV = 2 (1)

where k is the smoke extinction coefficient (m-1) and V is the visibility distance (m). Thus, 

measurement of smoke opacity or obscuration is useful in determining the ability to escape or 

perform needed action in a space during a fire incident. However, opacity is the result of the 

generation of the smoke and not a direct measure of its generation. Opacity results not only from 

the generation of smoke, but also from agglomeration and surface deposition during transport. 

Still, there are a number of widely-used tests that measure smoke opacity. 
26

Smoke opacity tests are broadly categorized as either static tests (those in which the smoke 

generated is allowed to accumulate within the test enclosure) and dynamic tests (those in which 

there is a continuous flow of gases resulting from combustion of the sample). 

The Smoke Density Chamber (ASTM E 662) [37], is used widely in testing of materials. 

Outlined in Figure 5, it is a static test that measures smoke generation from small, solid 

specimens exposed vertically to a radiant flux level of 25 kW/m2

 in a flaming (piloted ignition) 

or non-flaming mode. The smoke produced by the burning specimen in the chamber is measured 

by a light source – photometer combination. The attenuation of the light beam by the smoke is a 

measure of the optical density or “quantity of smoke” that a material will generate under the 

given conditions of the test. Two measures are typically reported. DS is an instantaneous 

measure of the optical density at a particular instant in time and is expressed as 

ܦௌ ൌ ܸ

ܮܣ log ൬

଴ܫ

ܫ

൰ (2)

where V is the volume of the chamber (m3

), A is the area of the exposed sample (m2), L is the 

path length of the light beam through the smoke (m), I0 is the intensity of the light beam before 

the start of the test, and I is the intensity of the light beam during the test. The maximum optical 

 Photodetector

 Light beam

 Infrared radiator

 Specimen 

 Six tube burner

 Trough for

 specimen melt

 Light source

Photometer

Figure 5. The smoke density chamber, ASTM E 662. 
27

density, Dm, is used primarily in ranking the relative smoke production of a material and in 

identifying likely sources of severe smoke production. Concerns with the test include the 

relatively low heat flux exposure, vertical sample mounting, and oxygen supply within the closed 

test cabinet [38]. Several researchers have concluded that tests like the Smoke Density Chamber 

do not provide a representation of the smoke emissions to be expected in real-scale fires [39–42] 

The International Organization for Standardization Smoke Chamber Test, ISO 5659 (also 

standardized as ASTM E 1995), shown in Figure 6, uses the same closed test chamber as the 

ASTM E 662 test, but with an improved specimen holder and exposure system [43,44]. The test 

apparatus includes a conical heater that can provide a heat flux level as high as 50 kW/m2 to a 

75 mm (3 in) by 75 mm (3 in) horizontal test specimen. Either flaming or non-flaming ignition 

is supported. Like the ASTM E 662 test, opacity measurements are with a vertically-oriented 

photometric system. In addition, mass optical density can be obtained with an optional load cell 

that continuously monitors the mass of the test specimen. 

While the test retains the limitations of a closed chamber like the ASTM E 662 test, it provides a 

more uniform sample heating that can be varied over a wider range to provide more realistic 

exposure. In addition, the load cell permits direct measurement of mass optical density. 

Figure 6. The ISO 5659 smoke density chamber with inset showing conical radiant 

heater. 
28

Dynamic tests which measure smoke obscuration have typically evolved from existing test 

methods that measure other fire properties such as heat release rate. These include the Ohio 

State University (OSU) calorimeter, ASTM E 906 [45], and the cone calorimeter, ASTM E 1354 

[46]. 

The ASTM E 906 apparatus, Figure 7, is used largely for aircraft applications. The test exposes a 

vertically- or horizontally-oriented specimen to radiant heat. Sample ignition may be nonpiloted, by ignition of evolved gases, or by flame impingement on the surface of the sample. The 

sample is contained within a chamber through which a constant flow of air passes. Measurement 

of the temperature change and opacity of the gas leaving the chamber allows determination of 

the rates of both heat and smoke release as the specimen burns. While an upper limit for sample 

exposure heat flux of 100 kW/m2

 is specified in the standard [45], difficulties are noted with heat 

fluxes above 50 kW/m2

 [47]. Specimen size is typically 150 mm (5.9 in) by 150 mm (5.9 in), 

but may be reduced if specimen heat release rate is large enough to allow flames into the hood of 

the apparatus. For smoke measurement, a photometer is incorporated on top of the exhaust hood. 

Issues with measurement of heat and smoke release rates have limited the usefulness of the 

apparatus and most work has transitioned to use of the cone calorimeter. 

The cone calorimeter (see Figure 8) makes use of an electric radiant heater in the form of a 

truncated cone, hence its name. The apparatus is general-purpose in that it may be used to test 

products for various applications. The heater is capable of being set to a wide variety of heating 

fluxes from 0 to 100 kW/m2

. The design of the heater was influenced by the ISO test for radiant 

ignition, ISO 5657 [48]. The technical features are documented in several references [49–52]. 

Some of the most salient features include: 

 horizontal or vertical specimen orientation, 

 composite and laminated specimens can be tested, 

 continuous mass loss load cell readings, 

 feedback-loop controlled heater operation, 

 HRR calibration using methane metered with mass flow controller, 

 smoke measured with laser-beam photometer and gravimetrically, and 

 provision for analyzing CO, CO2, H2O, HCl, and other combustion gases. 
29

Figure 8. The cone calorimeter, ASTM E 1354. 

Figure 7. The OSU calorimeter test, ASTM E 906.
30

The cone calorimeter is standardized as ASTM E 1354 [46] and ISO 5660 [53]. Smoke 

obscuration in the cone calorimeter is measured by a laser-based smoke measurement system in 

the exhaust stream. Smoke is reported from the test as the specific extinction area, the product of 

the extinction coefficient and volumetric flow rate divided by the mass loss rate. 

Hirschler [54,55] and Grayson [38] provide excellent critiques of bench-scale smoke 

measurement. 

3.2 Corrosion Test Methods 

A number of test methods have been developed and standardized for testing the corrosive hazard 

due to smoke. While the study of corrosion due to combustion products is certainly not new 

[56,57], the effort to develop a modern test method is fairly recent [58]. Initially, testing of the 

corrosivity of fire effluent was based on indirect measurements such as the amount of 

halogenated acids the fire effluent produces, the pH, or conductance of the fire effluent. While 

the tests are relatively straightforward to perform, there is currently no means to take the data 

from any of these indirect standards and estimate corrosion damage in a real fire. The inherent 

limits of indirect methods have resulted in the development of a number of direct methods to 

measure corrosivity of a test material’s smoke. Direct methods expose a test probe directly to the 

smoke and measure the amount of corrosion that occurs. 

After the 1974 electronic system fire in Poitiers France, the Centre National d'Études des 

Télécommunications (CNET) developed what is considered the first modern test of corrosivity 

[59]. In 1987, ASTM committee E 5.21.70 and the International Electrotechnical Commission 

(IEC) committee SC 50D each held initial meetings with the objective of developing standard 

corrosion tests. Initially the ASTM 5.21.70 committee developed ten criteria for an acceptable 

test for corrosion [60] as follows: 

1. Test should measure performance 

2. Combustion module should simulate real fire energies and growth rate 

3. All products should be tested in the same manner 

4. Combustion conditions should be capable of being varied 

5. The exposure module should reflect real life conditions 

6. The exposure target should be capable of being varied 

7. Protocol should allow a reasonable time between exposure and measurement 

8. Protocol should consider transport of the combustion products and their decomposition 

on the target surface 

9. Test protocol should not require excessively long use of equipment or operator time 

10. Test equipment should be relatively low priced. 

 

IEC SC 50D first considered the matter of corrosion in 1982 but it wasn’t until 1987 that IEC SC 

50D WG 3 [61] held its first meeting, which in part addressed the issue of the corrosivity of fire 

effluent. They began preparation of a draft summary of the future guidance document on 

corrosivity. Subsection titles from their initial report suggest important factors in the test method 

as follows: 
31

 Relevant fire models 

 Relevant corrosion targets 

 Effluent transport 

 Scaling factor 

 Relevant small scale direct tests 

 Development of derived (short time, inexpensive, correlatable) test methods for routine 

quality control 

 Damage both in room of fire and remote in space and time to fire 

 Misuse of tests and test data 

As both of these lists suggest, corrosion is a complex process, and developing an ideal test for 

the corrosivity of smoke from fires requires broad expertise. 

In the early 1990s, a number of tests using direct measures of corrosion were developed. In 

addition to the CNET test, the cone corrosimeter and the traveling furnace tests were developed. 

An additional direct test was developed by the ASTM E 05.21.70 committee but it was 

eventually withdrawn. Because the ASTM E 05.21.70 developed test figures prominently in the 

literature it will also be discussed in this section. In this section, test methods for corrosion will 

be described and analyzed. 

Recent research concluded that the largest risk to electrical circuits during a fire incident in NPPs 

is due to bridging of circuits [11]. While this is a serious issue, it has yet to garner much attention 

in the fire protection community. The last subsection will address how well existing corrosion 

tests do to predict bridging and what correlations may or may not exist between other fire tests 

for wire and cable. 

3.2.1 Indirect Methods 

All the standards for indirect methods of analysis to be described share a basic framework. The 

effluent from a burning sample is bubbled through some liquid to capture gases. The liquid is 

then analyzed and the properties reported. The acidity of the effluent is considered important, 

and because corrosion is an electro-chemical process, the conductivity of the liquid is often also 

considered. There are two types of indirect tests, one specific to halogenated acids and a second, 

general type that looks at pH and conductivity. Indirect methods can only address ASTM 

requirements [60] 1, 2, 9 and 10 directly. While correlations with damage, a strong theoretical 

understanding, and modeling capability could possibly make indirect methods the preferred test 

methods, currently such correlations and understanding do not exist. For this reason indirect 

methods have fallen out of favor as a tool to help address corrosion of fire effluent. 

3.2.1.1 Tests for Halogenated Gases: IEC 60754-1 and EN 50267-2-1 

Based on experience with real fires, halogenated plastics and halogens in general have been 

recognized as an important cause of corrosion. For that reason, there are a number of standards 

that focus on strength of the halogenated acids other than fluoric acid. They do this by using a 

chemical titration method that is specific to halogens instead of the general pH of a solution. 
32

IEC 60754-1 [62] and EN 50267-2-1 [63], both essentially the same standard, determine the 

generation rate of halogenated acid produced by a test sample. The standard states that for 

accuracy this method should not be used for samples containing less than 5 mg/g equivalent of 

HCl. Values are reported as the equivalent milligrams of HCl produced by 1 g of the sample. 

A test sample of 500 mg to 1000 mg is heated in a tube furnace at a uniform rate for 40 minutes 

until the sample’s temperature is 800 oC (1472 oF). It is then kept at that temperature for 20 

minutes of the actual test. A constant airflow is supplied to the furnace and then bubbled through 

two wash bottles of 0.1 M sodium hydroxide solution (NaOH). After the solution has cooled it is 

titrated using a wet chemistry method specifically meant to determine the amount of halogen 

acid in the solution and the results are transformed into an equivalent HCl mg/g production rate. 

3.2.1.2 Tests for pH and Conductance: IEC 60754-2, EN 50267-2-2 and EN 50267-2-3 

The more general pH tests are generally the same as for the halogenated gases except that the 

analysis is done with a general pH method and an additional test is done to measure the 

conductance of the solution. 

IEC 60754-2 [64], EN 50267-2-2 [65] and EN 50267-2-3 [66] use the same test apparatus as the 

halogenated gases, but the effluent is bubbled through two wash bottles of 450 mL of deionized 

water. The furnace is set to at least 935 C (1715 oF) and run for only 30 minutes with no initial 

heating phase unlike the halogenated version of the test. 

At the conclusion of combustion, IEC 60754-2 and EN 50267-2-2 combine the wash bottles and 

test the pH and conductivity using appropriate equipment. The values of two replicates are 

averaged and reported. Annex A of EN 50267-2-2 recommends that if the pass/fail criteria is not 

specified, the average pH should be greater than 4.3 and the conduction should be less than 

10 S/mm. 

For EN 50267-2-3, the reporting is different. Each material component of a cable or other 

application is tested with three replicates. The mean and standard deviation are determined and if 

the relative standard deviation is larger than 0.05, an additional three replicates are done and the 

mean and standard deviation of all six is used. Next the weight per unit of length for each 

component is measured and the weighted pH is calculated using 

ܪ݌ᇱ ൌ logଵ଴ ቌ ∑௜ ݓ௜

௜ݓ ∑

10௣ு೔ ௜

ቍ (3)

where wi is the weight of the ith component and pHi is the pH for that component. The weighted 

conductance is calculated using 

ܿᇱ ൌ ∑௜ ܿ௜ݓ௜

௜ݓ ௜∑

(4)

where ci is the conductance for the ith component. 
33

3.2.2 Direct Methods 

Direct methods test the effect of fire effluent directly on test samples. The push for direct fire 

corrosion tests comes from observation that fires can generate corrosive atmospheres even if they 

do not generate acid gases [67, 68]. While polymers containing halogens and producing acid 

gases such as HCl or HBr have been shown to cause extensive corrosion damage, many other 

materials such as woods, wool and polymers that contain nitrogen have also been shown to cause 

corrosion damage, at times worse than halogenated acids, while not producing halogenated or 

any other type of acids [69]. Besides measuring the corrosion caused by smoke, a second 

difference between indirect methods and direct methods is that direct methods can also 

determine the time dependent aspect of corrosion including the impact that may occur hours, 

days or even months later. 

After the 1974 electronic system fire in Poitiers France, CNET developed what is considered the 

first modern test of corrosivity [70]. A number of other standards have since been developed that 

utilize a variety of fire and exposure models as well as several different methods of reporting 

results. They generally use the same principle for measuring corrosion, which is to use the 

relationship between the thickness of a conductor and its resistance. The principle for making 

this measurement will be given and analyzed later. 

A common element of all direct tests is a combustion source used to generate the effluent which 

is exposed to a test probe for a period of time. The test probe is then kept in a controlled 

environment (for typically 24 h) at a specified temperature and relative humidity. Test 

measurements usually look specifically at the loss of metal from the test probe. 

All the direct tests use the same general method to measure the loss of material due to corrosion. 

The resistance of a conductor is related to its physical dimensions by 

ߩൌܴ

݈

(5) ܣ

where R is resistance,  is the resistivity of the material, l is the dimension in the direction of the 

current and A is the cross sectional area of the material. For a rectangular cross section, A = wh, 

where w is the width and h is the height. If the only exposed surface is the top of the conductor, 

then any change in resistance can be related to the amount of material that is removed by 

corrosion from the top resulting in an increase in resistance of the conductor. 

Direct test methods are broken into two types, static and dynamic. Test methods of each type are 

described below. 

3.2.2.1 Static Methods 

Tests are referred to as static tests if all the fire effluent is captured and held during the test. 

Generally the effluent is captured in the exposure chamber with the target present from the 

beginning of the test. Capturing all the effluent allows for the target to be exposed for a set 

period of time that can be significantly longer than the burning time of the sample. Static tests 
34

also make it easier to control the ambient conditions of the test such as the temperature of the gas 

and setting the relative humidity of the test chamber. The test emulates electrical equipment in 

the upper layer of the room of fire origin. 

 

3.2.2.1.1 ISO 11907-2, Plastics -- Smoke generation -- Determination of the corrosivity of fire 

effluents -- Part 2: Static method 

CNET in France developed what is generally considered to be the first modern corrosion fire 

test. This test method has been standardized as ISO 11907-2. The basic principle of the test as 

the standard states is “combustion – condensation – corrosion” [71]. 

The test chamber is a 20 L (0.7 ft3

) tube with a diameter of about 300 mm (11.8 in). One end has 

a sample holder where approximately 600 mg of the test sample is ignited and burned. At other 

end, a water-cooled test target holder keeps the target 10 C below the chamber temperature to 

encourage condensation on the test target. The test target is made up of 36 conductor lines with 

dimensions of 52 mm (2 in) long by 0.3 mm (0.01 in) wide by 17 m thick on a laminated epoxy 

circuit board. The nominal resistance, pre-test, is 8.0   0.5 . The reported value for the test is 

the percentage change of the resistance of the test target. An initial resistance Ri is taken before 

the test, and at any time t, the resistance is again measured giving Rf. The values are plugged 

into the following equation, which corrects for variations in initial resistance, to give the test 

value 

ܴ௖௢௥ ൌ 100 ቆ ܴ௜ܴ௙

8൫ܴ௙ െ ܴ௜൯

െ 1ቇିଵ

(6)

The derivation of this equation is given by Bottin [72]. 

Test chamber conditions are set to 50 oC (122 oF) and 65 % relative humidity with the watercooled test target set to 40 oC (104 oF). The test sample is put in an inert crucible in the sample 

holder with the heating wire at 800 oC (1472 oF) and kept at that temperature for 3 minutes. After 

60 minutes from the time the sample is placed in the sample holder, the final reading of 

resistance is taken, and the test target is removed from the chamber. 

By using the percent change in the resistance as the reported value of the standard, the CNET test 

has a nonlinear relationship between the reported value and the amount of corrosion that occurs. 

The CNET categories are at 10 %, 20 % and 30 % change in resistance. Using the above 

equation, it can be seen that a 10.0 % increase in resistance would mean only 9.1 % of the 

conductor had been lost to corrosion, a 20.0 % increase would indicate a removal of 16.7 % of 

the conductor and a 30.0 % increase would mean only 23.1 % of the material had been lost to 

corrosion. 

3.2.2.1.2 ASTM E05.21.71 (withdrawn) 

A second static test underwent a significant amount of development in ASTM E05.20. However, 

after ASTM D5485 was approved, development on ASTM E05.21.71 was discontinued and the 
35

standard was withdrawn. Since a great deal of work was done in the development of publications 

and test data referencing the standard, it is important to describe the test method. 

ASTM E05.21.71 starts with the “NIST tox box” as the exposure chamber, which has a volume 

of 200 L (7 ft3). It uses a cylindrical quartz combustion cell that is connected to the exposure 

chamber by a stainless steel lined flue. Exposure ports are used for probe instrumentation and an 

additional port is connected to a 49 L (1.7 ft3

) plastic expansion bag for pressure relief. 

Test sample sizes were not standardized, but the samples were intended to be small enough such 

that combustion would not be oxygen limited. Test probes were manufactured by RohrbackCosasco. The basic configuration was of two legs of copper. One leg is shielded from the 

effluent and used as at the reference. The other leg is exposed and is the measurement leg. 

The test procedure used by Kessel, et al. [73] to expose the test sample places the specimen 

holder in the furnace and the furnace and test chamber are sealed. The atmosphere in the 

chamber is brought to 60 % relative humidity, the furnace heaters are set to 50 kW/m2

, and the 

spark igniter is turned on and left running for 15 minutes. After 15 minutes, the spark igniter is 

turned off and the flue to the test chamber closed. The test probe is then left in the test chamber 

for another 45 minutes. The probe is then removed from the test chamber and put into an 

environmental chamber with 75 % relative humidity for 24 hours, and finally, put in to a second 

environmental chamber with 35 % relative humidity for six days. 

Measurements are made every 2 minutes to 3 minutes during the first hour, after 24 hours in the 

first environmental chamber and after the six days in the second environmental chamber. 

3.2.2.2 Dynamic Methods 

Dynamic methods differ from static methods in that the exposure model has a continuous flow of 

effluent and does not collect and hold all the effluent for the test duration. 

3.2.2.2.1 ISO 11907-3, DIN 53436, Plastics -- Smoke generation -- Determination of the 

corrosivity of fire effluents -- Part 3: Dynamic decomposition method using a 

travelling furnace 

The traveling furnace test uses an annular furnace that has a 100 mm (3.9 in) exposure area. The 

furnace is set up using a 1 m quartz glass tube with an outer diameter of 40 mm  1 mm and a 

wall thickness of 2 mm  0.5 mm. The test sample is placed in a quartz glass cuvette that is 400 

mm  10 mm long and 15 mm  1 mm high with a wall thickness of 1.7 mm  0.2 mm. The test 

sample preparation differs depending on the type of material but it approximately fills the 

cuvette. 

The test probe is the same as the one used for the CNET tests and like the CNET tests is mounted 

on a water cooled specimen holder to enhance condensation. It is placed so the center of the 

probe is 200 mm (7.9 in) from the downstream end of the test sample cuvette. 
36

The test procedure is to place the sample in the cuvette and place the cuvette in the quartz tube so 

that the first 100 mm (3.9 in) is in the exposure zone of the furnace. Using room air, a flow 

through the tube of at 100 L/h  5 L/h is established. The furnace is set at 600 C  20 C using 

the calibration curve previously determined with the reference body. The furnace then travels at 

10 mm/min  0.5 mm/min until it reaches the other end of the test sample, which should take 30 

minutes. 

Within 5 minutes of the end of the test the test probe is to be placed in an environmental chamber 

at a constant 23 C  2 C and 75 %  5 % relative humidity. Resistance measurements are made 

at one hour and 24 hours after the start of the test and are reported using the same calculation as 

the CNET tests. 

By using a fire model of assisted opposed flow flame spread, the traveling furnace does not 

model flame spread typical of real fire scenarios, but it is likely a more reproducible fire 

environment. Ideally, the test probe is exposed to a quasi-steady state flow including products 

from ignition through to burnout. Having quasi-steady state conditions for most of the 30 

minutes of the dynamic part of the test should increase repeatability and reproducibility, which if 

results can be correlated with real scale fire damage allow meaningful ranking of materials. 

 

3.2.2.2.2 ASTM D5485, ISO 11907-4, Standard Test Method for Determining the Corrosive 

Effect of Combustion Products Using the Cone Corrosimeter 

The cone corrosimeter is designed to be an attachment for the well-established fire performance 

test, the cone calorimeter. The general idea of the corrosimeter was first published in 1990 by 

Ryan et al. [74]. 

The corrosimeter attaches to the cone calorimeter above the cone furnace. It starts with a metal 

funnel above the cone to concentrate the effluent. One end of a rigid, heated, stainless steel tube 

is placed in the upper narrow opening of the funnel with the opening pointed up away from the 

burning test specimen so that the opening doesn’t become clogged with soot. The other end of 

the 675 mm  75 mm tube is connected to a flexible heat-resistant tube that is 255 mm  10 mm 

long and connects to the exposure chamber. The exposure chamber is 11.2 L  0.5 L with an 

inlet and outlet port and an O-ring sealed top to allow the test probe to be placed in the chamber. 

The outlet port is connected to sufficient filtering to protect a pump that draws the air through the 

exposure chamber to be released into a hood or other exhaust handling equipment. 

To test a material or configuration of materials requires five samples. The first two samples are 

run in the cone calorimeter without the corrosimeter to determine the average time to 70 % mass 

loss. The final three samples are burned with the corrosimeter attached. The flow through the 

exposure chamber is set at 4.5 L/min. The stainless steel tube is heated to 105 C (221 F). The 

flux from the cone heater is set at the desired value and the material is ignited. Gas from the 

effluent is drawn until the previously determined 70 % of expected mass loss is achieved. At this 

point the intake and outlet ports are closed off and the target probe’s exposure continues until an 

hour after the beginning of the test. At this point the target probe is tested to determine the 

change in resistance, and then the target probe is placed in an environmental chamber with 23 C 

 2 C and a relative humidity of 75 %  5 % for 24 hours, after which the change in resistance 
37

is again measured. To calculate the amount of metal, the standard directs the tester to refer to the 

procedure provided by the target probe’s manufacturer. 

While the cone corrosimeter is defined as a dynamic test, it has aspects of both a dynamic test as 

well as a static test. 

3.2.3 Analysis of Individual Standards and Test Methods 

Before looking at work done in support of the standards described earlier, it is important to 

understand what is missing. The most important fact to understand about all the standards is that 

they only provide a rank ordering of materials. While it is possible to establish classification 

values on the results of each of the standards, there is currently no work that relates the standards 

to large-scale testing. Babrauskas and Peacock [75] argue that what makes the cone calorimeter 

useful for fire protection is that performance in the cone can be related to full scale burns and 

real fires. The lack of large-scale testing for corrosion implies there is not an equivalent basis for 

corrosion performance criteria. The best that can be done is to provide a relative ranking of 

material performance and set performance criteria that would exclude undesirable materials from 

selection. However, just because a material is relatively noncorrosive in one or all of the benchscale tests does not necessarily imply that it will exhibit similar properties in a full-scale fire. 

Thus, there needs to be bench- to large-scale comparisons for the data to be useful for more than 

relative comparisons. 

The Polyolefins Fire Performance Counsel (PFPC) performed a study of four test methods and 

published the results in five papers [73,76-79]. The first four reviewed the work on each of the 

test methods, the Radiant Panel, the CNET test, the modified DIN indirect test method and the 

cone corrosimeter. The final paper discusses and compares the test methods. For completeness, 

the 25 materials tested by the PFPC authors are included here as Appendix A. 

There is little in the literature discussing indirect test methods other than simple test method 

descriptions. The measurement methods use well-developed wet chemistry methods. However, 

Saitoh and Inukai [80] used these wet chemistry methods to look at the effect of burning chlorine 

containing materials on the corrosion of steel and stainless steel plates. Saitoh and Inukai burned 

1.0 g samples of various carpet tiles for three minutes in a quartz tube furnace set to either 550 

C (1022 F) or 750 C (1382 F). Airflow of 1 L/min was supplied at one end and the flow of 

air and effluent was bubbled through an absorbtion bottle of 0.1N NaOH to capture the HCl, and 

the production rates of HCl were determined. 

Using the same furnace and procedures, identical samples were burned, but the furnace was 

connected to an exposure chamber where plates of steel and stainless steel were mounted in 

horizontal and vertical orientations. After a 30 minute exposure the plates were stored in an 

environmental chamber kept at 20 C (68 F) and relative humidity of 80 %. After one, two, and 

four weeks, the amount of corrosion was determined although all corrosion data reported is after 

four weeks. 

As can be seen in Figure 9(a) and Figure 9(b), the corrosion of the steel plate seems to be 

correlated with the production rate determined for each test sample even though the production 
38

rate and corrosion rate were generated from separate experiments; however, the corrosion of the 

stainless steel plates has no clear correlation with production rates. While the data for the 

production rate of HCl and the corrosion of the metal were conducted separately, it is clear, at 

least for the steel plate, that the results of an indirect test can be related to corrosion, but the 

stainless steel test shows that the correlations don’t hold for all materials. 

(a) Steel Plate Corrosion 

(b) Stainless Steel Corrosion 

Figure 9. Comparison of corrosion on plain and stainless steel plates after exposure to fire 

smoke. Mass loss typically determined by conductive wire resistance change over 

time [80]. 

HCl Production Rate (mg/g)

0 50 100 150 200 250 300 350

Mass Loss After 4 Weeks (mg/cm2

)

0

2

4

6

8

10

12

14

Horizontal 550 

Vertical 550 

Horizontal 750 

Vertical 750 

Vertical 550 Outlier

HCl Production Rate (mg/g)

0 50 100 150 200 250 300 350

Mass Loss After 4 Weeks (mg/cm2

) 0.0

0.2

0.4

0.6

0.8

1.0

1.2

Horizontal 550 

Vertical 550 

Horizontal 750 

Vertical 550 Outlier
39

Saitoh and Inukai contend that humidity is probably the most important factor in determining the 

amount of corrosion that occurs [80]. They also note that the combustion gases from materials 

such as wood and asphalt that are not expected to produce HCl still produce corrosion. They 

surmise the presence of other gases besides HCl, which questions the value of test methods that 

only look for HCl or specific halogen acids. 

Both IEC 60754-1 and EN 50267-2-1 do not specifically test for the presence of HF. Sandmann 

and Widmer [81] looked at the effect of fluoride on stainless steel. They found that the fluoridecontaining compounds tested were very stable thermally. They also found that even when the 

compounds did give off fluoride, the resulting effluent was significantly less corrosive than other 

halogens like chloride (except for a single test with carbon steel as the target). They noted that 

HF was significantly less corrosive to copper and silver than HCl was. This seems to contradict 

Tewarson [19] where HF was found to be significantly more corrosive than HCl. The difference 

may arise from the target being used for measurement, the method of measurement or the actual 

environments and possible all three. Tewarson used a steel probe that was put in a solution of the 

fire effluent in water and measured the corrosion using change in resistance. Perhaps the only 

conclusion to be drawn is that test conditions can significantly impact observed corrosion. 

 

The CNET test has existed in some form since at least 1983 [82]. It is used as a comparison 

standard and as such is discussed as it relates to other tests, but there is little work that focused 

directly on the standard. Rio and O’Neill [59] described the test and presented test data for 12 

materials that have corrosion values ranging from near 0 % increase in resistance to close to 15 

%. They define the repeatability qualitatively as “reasonable.” 

The PFPC study used the CNET test as one of its four standards for comparison [76]. They found 

that the test method did not differentiate the materials particularly well. One modification of the 

test method that was used was to add 100 g of polyethylene (PE) to the 600 g of test material to 

ensure complete combustion. Even with the PE, they found that the completeness of combustion 

and variation in the percent of mass combusted is significant. One possible source for the 

problem of complete combustion was the three minute heating cycle, which was deemed to be 

too short. They noted that weight loss seemed to stop for most materials at the end of the three 

minute period. They also found that for the test probe specified in the CNET test, the risk of 

bridging between the conductor lines was significant. They showed pictures of two probes after 

tests that seemed to show some bridging occurring. They also had two tests where the resistance 

didn’t increase but decreased, indicating significant bridging had occurred. Finally, only two of 

the 24 test materials were found to be statistically more corrosive than the rest. 

There is little in the literature about the traveling furnace test used as a smoke corrosivity test. 

The apparatus has been extensively used and studied in the toxicity test as part of DIN 53436. 

Prager et al. [83] and Prager [84] evaluated the test method in DIN 53436, the traveling furnace, 

and found that it could properly simulate smoldering and flaming fires. Its utility is demonstrated 

by its use to collect fire test data on toxicity in developing a significant life-cycle assessment 

model [85]. Barth et al. [86] concluded that the traveling furnace could also be used for corrosion 

testing. It is seen to have a number of positive attributes including control of combustion for both 

flaming and smoldering fires. It can generate a relatively constant smoke stream over an 
40

extended period or a dynamically changing smoke stream and the composition can be 

characterized at different times during combustion. 

Ryan et al. [68] suggested using the cone calorimeter to resolve several problems they found 

with other test methods they analyzed. First they wanted to address the ASTM E05.21.71 task 

group’s criteria for a bench-scale corrosion test, second, include standard samples of electronic 

components and circuits, and finally, to include the effect of corrosion on metal loss, circuit 

bridging, and degradation of electrical contacts. They considered a number of options including 

using a single chamber for combustion and exposure or dual chambers, using flow-through or 

closed design and other design parameters. The design they discussed is broadly similar to the 

standardized cone corrosimeter design, but is significantly different in details. The design 

purposed used a syringe style extraction method in the duct above the exhaust fan of the cone. 

The exposure chamber was completely closed. The actual standard as described before has a 

hybrid open/closed system that draws effluent above the cone radiator, but below the exhaust 

fan. 

The PFPC ran tests using a development version of the cone corrosimeter [78]. The most 

significant difference between the test method used by PFPC and the one in the standard is the 

rate of airflow. The stated airflow the PFPC used was 0.024 m3

/s, which is 320 times the 

0.000075 m3/s in the ASTM cone corrosimeter standard and would cause an air change of 

0.0112 m3

 in less than 0.5 s. There is no way to determine what airflow rate was actually used 

from the papers. It is possible they used 0.024 L/s, which would be 0.000024 m3/s, much closer 

to the standardized value. In the PFPC tests, both 2500 Å and 45000 Å probes were used and 

tests were conducted at both 25 kW/m2 and 50 kW/m2. The PFPC tests found a number of 

difficulties with the cone corrosimeter tests. Their first observation was that a brominated 

polyethylene was found to be less corrosive than three different materials containing fillers. 

Several samples bubbled out of the sample pan and invalidated the tests, which they felt needed 

to be corrected. Finally, they found a number of problems with the measurements the test 

provided. 

Most of the difficulties came from using the four separate measurement scenarios recommended 

in the annex of the standard. The standard doesn’t specify a particular heat flux and it doesn’t 

specify a thickness of target but suggests using the 250 nm (2500 Å) probe and/or the 4500 nm 

(45 000 Å) probe and fluxes of either 25 kW/m2

 or 50 kW/m2. The PFPC study used both probes 

together in test series at each flux level and found that there was a significant lack of consistency 

in the four scenarios. They made six runs with the 6th specimen material, three on one day and 

three on another day. They found that the repeatability was poor and that, interestingly, the 

results were strongly correlated by the day of test as can be seen in Figure 10. 
41

Figure 10. Observed repeatability for a material tested in the cone corrosimeter [77]. 

The correlation is even stronger than just by the day of test. Because each test had a 250 nm 

probe and a 4500 nm probe, the test-to-test correlation was strong as seen in Figure 11. The 

strength of the correlation seems to reinforce the variability in the performance of the material 

and not just uncertainty in the test measurement. Some possible explanations are offered in 

Appendix B. There is an issue with pitting that can overestimate the total corrosion of the 

effluent. This effect is increased with the use of the thinner probe. That would seem to account 

for the fact that 250 nm probes consistently read a higher level of corrosion. The other issue with 

the corrosimeter is that the hybrid dynamic/static nature of testing makes it sensitive to 

differences and variability of HRR between materials and tests. The strong correlation with the 

day the test was run has no clear explanation. It implies that some variable that was not 

accounted for changed between the two days, but it is impossible to tell from the paper. 

Probe

250 nm 4500 nm

Corrosion Depth (nm)

0

500

1000

1500

2000

2500

3000

Day 1 

Day 2 
42

Figure 11. Comparison of test results in the cone corrosimeter at 25 kW/m2

 and 

50 kW/m2 for one material. Data from reference [77]. 

Grand [87] first discussed using a modified version of the NIST cup furnace used for toxicity 

testing [88, 89] as a test method for both corrosion and toxicity testing. The apparatus is able to 

determine an ignition time, rate of smoke evolution, total amount of smoke produced, and 

characterization of the smoke in terms of either toxicity or corrosivity. The test method’s 

flexibility in fire conditions as well as it being a closed system were listed as its key advantages. 

In 1991, Grand [90] proposed a modified version of the original proposed test focusing on 

corrosion. A copper probe using resistance to measure metal loss was added to the system. The 

system was tested with six plastics: 

 Ethylene-vinyl acetate (EVA) 

 Ethylene-vinyl acetate with fire retardant using red phosphorus (FR-EVA) 

 Low density polyethylene (LDPE) 

 Low density polyethylene with fire retardant using red phosphorus (FR-6400) 

 Polyethylene with fire retardant using bromine (PE165) 

 Polyvinyl chloride (PVC). 

These tests were run using both 25 kW/m2

 and 50 kW/m2, irradiating the samples for 15 minutes 

in each test. The tests generated the expected results with PVC, clearly the worst material in 

both total metal lost and the rate of metal loss. The PE165 was a distant second and the pure 

EVA and LDPE were the best. Grand also showed that humidity increased the corrosion rate 

and total corrosion, as theory and experience predict [87]. 

Corrosion Depth, 4500 nm Probe (nm)

0 50 100 150 200 250 300

 Corrosion Depth, 250 nm Probe (nm)

0

10

20

30

40

50

60

70
43

Grand also showed time histories of the amount of metal lost in different tests. The utility of this 

information is clear from the very different shapes of the curves from different test materials. 

Some materials had a relatively high rate of corrosion that slowly decreased over time while 

other materials caused short but very rapid loss of material before sharply changing to a much 

slower rate of loss so that they looked almost like step functions. 

Grand summarized the development of the radiant panel test [91]. He argues that the radiant 

panel test is flexible and useful for characterizing the corrosivity of a material’s effluent. He lists 

five advantages of this system, which include: 

 Flexible combustion conditions 

 Capturing all fire effluent from the test 

 Multiple corrosion probes can be placed in the large test chamber 

 The method has proven an ability to distinguish between different polymer materials 

 Products can be tested in their end use. 

Grand also identified a number of fundamental research issues that needed to be addressed for all 

corrosion testing and not just the radiant panel. They included: 

 The response of resistance probes to hot, moist clean atmospheres 

 The repeatability of resistance probe measurements 

 The response of resistance probes to known quantities of known corrosive agents 

 The impact of orientation and exposure time on measurements 

 The importance of using metals besides copper in resistance probes. 

The PFPC also studied the radiant furnace test [73]. They found that the test differentiated 

between different types of polymers. The main concern expressed was the repeatability of the 

test. For a single material, they had three tests in which metal loss was between 15 Å and 30 Å, 

two with metal loss between 30 Å and 120 Å and one with metal loss measured at 784 Å. Even 

excluding the 784 Å case, the standard deviation was very high with a mean of 170 Å ± 303 Å 

including the 784 Å case, and 47 Å ± 42 Å excluding it. 

A gas analysis found that the minimum oxygen concentration was high enough to be assured that 

combustion was not oxygen limited. Looking at sample size, they found that increasing the mass 

did not increase the corrosion that occurred by the same factor. They also found that seven out 

of nine of the smaller samples didn’t seem to reach flaming combustion, but weight loss data 

showed a significant amount of decomposition did occur. 

Finally, because some of the test materials were able to corrode the 2500 Å probe beyond its 

maximum measurement capability, they also used probes of 25,000 Å copper foil. There seemed 

to be a linear relationship between the thicknesses of probes and corrosivity. They theorized that 

the copper foil had fewer lattice defects than the dc magnetron sputter-formed 2500 Å probes 

they used for all other tests. They note as described in Appendix B that increased pitting would 

significantly change the resistance even though little metal had actually been lost. 
44

3.2.4 Comparison of Test Methods 

As mentioned before, Hirschler and Smith [67] showed that all fires are corrosive and that it is 

not just acid gases that cause the corrosion. In this work that was originally presented in the 

October 1987 ‘Corrosive Effects of Combustion Products’ conference in London, the results of a 

number of experiments were shown. The work exposed steel coupons and copper mirrors in an 

ASTM E662 “NBS Smoke Density Chamber” to the effluent of a number of products for an hour 

and then weighed the amount of material that was lost to corrosion. 

While they did test copper mirrors, the primary focus of the work was the corrosion of steel. 

They were able to test the corrosivity of the same products in a number of environmental 

conditions. Corrosion of steel was measured by determining the amount of steel left after the 

exposure period. Two chamber temperature conditions were used, near ambient, and heated to 

between 100 C (212 F) and 110 C (230 F). In the near ambient tests, one coupon was placed 

on a bag of ice to enhance condensation. For the cases where the chamber was heated, one 

coupon was placed on a hot plate and warmed to 550 C (1022 F). Both test series had three 

untreated coupons in each test as well as a coupon that was pretreated with machine oil. Two of 

the three untreated coupons were treated a day later to simulate cleaning. All tests used a high 

humidity environment. 

The results showed that when conditions were varied, different materials tested as the most 

corrosive. While all materials tested had a corrosive effect on the targets, there was not a 

consistent pattern in the reaction of the steel coupons to the test conditions. Enhancing 

condensation with ice typically increased the corrosion though there were exceptions. Heating 

the coupons was seen to increase corrosion with increased reactivity with oxygen reported as the 

main reason for the corrosion. 

The pretreatment as well as post treatments generally seemed to work, but not always. The 

treatments, both pre and post, seemed to work better in the heated tests than in the ambient tests. 

One exception was a single test with a warm exposure chamber where the pretreatment seemed 

to cause a ten-fold increase in corrosion. All cases were found to render the copper mirrors 

useless as conductors. At ambient conditions, the materials that released the most HCl caused the 

most corrosion. While most of the copper in the mirrors remained after the tests, pitting left the 

mirrors useless as conductors. 

Finally, Hirschler and Smith [67] showed that water condensation greatly enhances corrosion. 

The significant sensitivity of corrosion to test conditions as well as the inherent corrosivity of 

fire effluent is a significant part of the reason for moving from indirect methods to direct 

methods. 

In 1988, Fallou [61] gave an overview of the subject and a review of activities over the previous 

ten years that the IEC had conducted on the corrosion issue. According to Fallou, it was 

generally agreed that it was desirable to be able to use preliminary tests to determine which 

materials were usable. The hope was that with application of the science of corrosion one would 

be able to use the results of bench-scale tests to determine full-scale behavior without having to 

run the experiments. Fallou listed three main concerns with corrosion of electrical equipment. 
45

The first concern was electrical contacts since experience in industrial atmospheres had 

demonstrated that even low level exposures could cause contacts to fail quickly. The second 

concern was the loss of metal conductor in circuits causing the circuit to fail. Thirdly, impact of 

corrosives on insulators which can lead to bridging or short circuits was a concern. 

In 1988, Briggs [92] reported on the status of the actual tests under development for three 

properties of smoke, density, toxicity and corrosivity. His main focus was on smoke density and 

smoke toxicity. He reports that the interests of the ISO/TC61/SC4/WG2 group were mainly in 

understanding the decomposition models, condensation techniques and corrosion detectors. At 

that time, the fire tests being considered were a Japanese system, DP5659, for measuring smoke 

density and the traveling furnace in DIN 53436. No specifics were offered on the work on 

exposure chambers. Finally, initial work on a corrosion probe would use the CNET probe. 

Hirschler gave a summary of the state of understanding of smoke corrosivity at the 1990 

International Wire & Cable Symposium [93]. He compared the results of two acid gas tests, the 

hot tube furnace used by the Canandian Standards Association and the “coil” test with the CNET 

probe. He noted that the acid gas tests give virtually identical results and that the CNET results 

“parallels” the acid gas results. He suggested that this is because the CNET test forced 

condensation, with no post exposure period and an unrealistically intense fire model. While the 

CNET results have the same trend as the acid gas tests, the results do not parallel the acid gas test 

results. 

Hirschler reviewed his and Smith’s work [67] described earlier, putting significant focus on the 

impact of heat on corrosion. He notes how heating the steel coupon to 550 C (1022 F) in a 

moist environment with the air heated to 100 C (212 F) to 110 C (230 F) causes a significant 

and relatively consistent level of corrosion. While the results are significant, it is not clear how 

realistic the scenario actually is. Hirschler notes that chlorine-generating materials are more 

corrosive in the cooler environment, possibly due to condensation. He also points out that 

nylon’s increased corrosivity in the warmer environment didn’t have an obvious explanation. 

As the first of the direct test methods, the CNET test is a benchmark used for comparison of 

other tests. Bottin showed that the CNET method was an appropriate method to measure 

corrosivity of fire effluent [72, 94]. As part of the testing, Bottin compared the results of the 

CNET test to the conductivity of seven samples that were tested. The two samples containing 

fluorine were not tested for conductivity, but for the other five samples, only one product failed 

to rank the same for both tests, a flame retarded compound containing decabromodiphenyloxide. 

As can be seen in Figure 12, the four materials that did rank the same in both tests seem to be 

almost perfectly exponentially correlated. 

In 1991, Briggs [69] reviewed IEC 754-1 and IEC 754-2, which were standards at the time, as 

well as the traveling furnace and radiant panel tests, which were both in a development phase. 

The traveling furnace became IEC 754-3. The cone corrosimeter, which became IEC 754-4, is 

not reviewed. He discussed the concerns with corrosion testing at the time, which have largely 

remained unchanged, but didn’t review any data, old or new. He concluded that adequate testing 

methods had not yet been developed. 
46

Figure 12. Comparison of CNET test results with measurements of conductivity for five 

samples tested. Data from references [72,94]. 

Hirschler studied the available test data for smoke corrosion tests [95 - 97]. He described the 

CNET test, ASTM E05.21.71 draft radiant panel test, ASTM D09.21.4 cone corrosimeter in draft 

form and the DIN 53463 traveling furnace. He included all the tests that he reviewed in more 

detail in International Wire & Cable Symposium paper [93]. Added to this paper is a review of 

the ASTM E05.21.71 task force requirements with recommendations for two additional 

requirements4

: 

11. Test should be repeatable and reproducible 

12. Test results should correlate validly with those obtained from corrosion following 

full scale fires. 

He later looked at the four corrosion test methods of the time and considered how they 

performed compared to the requirements. He found the indirect tests do not meet most of the 

criteria. Hirschler thought that most of the problems with the CNET test can be easily resolved 

but the main problem is repeatability. Basically, there is not much information on the other tests. 

He reported that the DIN traveling furnace test was not defined well enough to evaluate although 

 

4 See page 30 for the original 10 recommended requirements for a corrosion test method from the ASTM E05.21.71 

task force. 
47

he stated, “the combustion module of this test is, however, generally considered as 

unrepresentative of real fire conditions, meaning criteria 2 would not be met”. He deemed the 

radiant panel and cone corrosimeter tests to meet criteria 1 to 7, but neither address criteria 8, 11 

and 12. 

Gandhi [98,99] performed some simple modeling of three types of gas collections systems that 

could be used in corrosion tests, the CNET test, the cone corrosimeter, and a third system that 

utilized a piston cylinder chamber. He used the mass fraction of an arbitrary corrosive 

component of the fire effluent, a, as an indicator of how each capture system works and 

developed design parameters for each test. However, the important quantity for determining 

corrosivity is the concentration. The nondimensionalized concentration measures for the three 

tests are also developed in Appendix C. For the CNET test, the concentration is much easier 

than the mass fraction and is simply 

௔ܥ݀

∗

݀߬ ൌ ݕ௔Γ୤

∗ (7)

where Ca

*

 is the nondimensionalized concentration,  is the nondimensionlized time, ya is the 

production rate of product a in units of kg of product a produced per kg of fuel burned and f

*

 is 

a nondimensionlized mass loss rate. Thus, at the end of the burning phase of the CNET test, the 

concentration of product a is dependent on the amount of product a produced by the material 

being tested. With one caveat, there is a very straightforward relationship between the test 

material and the concentration of a particular corrosive product. The caveat is that there is 

concern about the mass loss rate being limited by the available oxygen. 

To show how serious the concern about oxygen limited combustion is, assume that the oxygen 

lower limit is 15.5 %, then the maximum sample size that can undergo complete combustion 

given the stoichiometric oxygen to fuel ratio is calculable as shown in Figure 13. Note that the 

nondimensionalized mass of a test material in ISO 11907-2 is 1.0. A number of common 

materials could experience oxygen limited burning in the CNET test so some care must be taken 

with interpreting the results of the test. 
48

 

Modeling the cone corrisometer Gandhi makes two significant simplifications. The first is to 

assume that the test uses mass flow control instead of volume flow control and that the control is 

sufficiently good to maintain constant mass in the exposure chamber. The second is not so much 

a simplification as a potential for misunderstanding. Gandhi assumes that the amount of mass 

entering and leaving is related to the mass loss rate (MLR) by a fraction f. While there is no 

requirement for f to be a constant it is easy to make that mistake. To make the analysis easier, it 

is desirable to consider a constant mass flow (see details in Appendix C). Since the volume is 

constant and the assumption is the mass is also constant, then the mass fraction of product a, Ya, 

is also the nondimensionalized concentration and is given by 

௔ܥ݀

∗

݀߬ ൌ ݂௜௡

௔ݕ ቀ∗ 

1െߙ െ ܻ௔ቁ (8)

where fin

*

 is the nondimensionalized mass flowing into and out of the exposure chamber, Ya is 

the fraction of the mass in the exposure chamber that is product a and  is the rate of the mass of 

air entrained by the fire to the MLR. The term 

௔ݕ

(9) ߙെ1

represents the fraction of the total flow of mass, both effluent and entrained air, generated by the 

test sample in the cone. This term will overestimate the fraction of the mass flowing into the 

Stoichiometric Ratio of Oxygen to Fuel

0123456

Maximum Sample Size 

(nondimensionalized mass)

0.0

0.5

1.0

1.5

2.0

2.5

15.5% Oxygen lower limit

Materials

PVC

Nylon

Polystyrene

Polyethylene

Methane

Figure 13. Maximum sample size for given oxygen fuel ratio assuming complete 

combustion. 
49

exposure chamber at points where the total mass flow from the product is less than the forced 

flow of the pump, but should not be a significant error. 

The fifth paper by the PFPC compared the results of the four standards and performed extensive 

analysis [79]. They reviewed the entire project and then did an overall analysis of the results. 

They looked at three factors in the comparison and analysis: 

1. Precision – Is the test repeatable? Does the test differentiate corrosive potentials? 

2. Accuracy – Does the test differentiate corrosive potential consistent with known 

chemistry? Are the test results consistent with existing standards? 

3. Cost, availability and convenience – Is the test equipment accessible, easy to operate and 

mechanically sound? 

To assess repeatability, they looked at the average coefficient of variation (the standard deviation 

divided by the mean expressed as a percentage), as well as the standard deviation of the 

coefficient of variation. Their results are given in Table 8. 

Table 8. Repeatability of several corrosion standards. Data from reference [79]. 

Test Average Coefficient of 

Variation 

Standard Deviation 

of Coefficient of 

Variation 

ASTM E05.21.71 86.0 42.3 

CNET 51.8 27.1 

DIN Conductivity 11.4 8.95 

pH 5.21 4.65 

ASTM 

D09.21.04 

50 kW/m2 45 000 A 37.0 31.2 

50 kW/m2 2500 A 22.2 22.8 

Clearly the indirect tests were the most repeatable of all the tests. None of the direct tests had a 

particularly low average coefficient of variation. The question becomes are they sufficiently 

repeatable. To answer this question they used two statistical tests to see how many statistically 

differentiated groups each test could break the 24 products into. CNET differentiated product 20 

into one group, product 19 into a second group and the rest into a final group. 

Overall, they found that none of the four test methods satisfied all the criteria for a useful 

corrosion test. Since the tests did not give the same rankings they were not interchangeable. They 

recommended that both the cone corrosimeter and the radiant panel needed to have their 

repeatability improved and that development on the CNET test should stop. 

 

51

4 MODELING OF SMOKE GENERATION, TRANSPORT, AND 

DEPOSITION 

4.1 Use of Smoke and Species Yields as Model Inputs 

While there are detailed combustion models available that fully address gas-phase chemistry, 

they are not practical for the large domains encountered in typical fire scenarios. As such, 

modeling of chemistry in most current computer fire models is not considered in detail beyond a 

one-step effective reaction and is largely a bookkeeping exercise based on a simple reaction of 

fuel and oxygen such as shown below [100]. 

ܥ௩ܪ௪ܱ௫ܰ௬ܥ݈௭ ൅	ߥைమܱଶ

ܰܥܪே஼ுߥ ൅ ݈ܥܪ௟஼ுߥ ൅ ܰ2ேమߥ ൅ ௌSootߥ ൅ ܱܥை஼ߥ ൅ 2ܱܪுమைߥ ൅ ଶܱܥைమ஼ߥ →

For complete combustion of the simplest hydrocarbon fuel, methane reacts with oxygen to form 

carbon dioxide and water. The only input required is the pyrolysis rate and the heat of 

combustion. For fuels that contain oxygen, nitrogen, or chlorine, the reaction becomes more 

complex. In this case, the user specifies model inputs for the composition of the fuel and any 

non-ideal combustion yields (such as the production of soot or carbon monoxide) to allow the 

model to calculate the mass of species produced during combustion. Most typically, these are 

specified as molar yields (i.e., the number of moles of a given species produced per mole of fuel 

consumed in the combustion reaction), though other normalized values are also used5

. For 

example, for soot, the effective molar yield, νS, is related to the soot yield, yS, via the relation 

ߥௌ ൌ ܹ௙

ܹௌ

(10) ௌݕ

where Wf and WS are the effective molar mass of the fuel and soot, respectively. In most cases 

these are idealized estimates for actual complex fuels. 

The total amount of a given species released by a fire is thus dependent on the fuel consumed. 

This is most typically specified as a user input based on a combination of the burning object’s 

heat release rate (ܳሶ), mass loss rate (݉ሶ), and heat of combustion (Hc) related as ܳሶ ൌ ݉ሶܪ௖. The 

discussion above is essentially book-keeping, the accounting of the gas molecules formed in the 

combustion process using estimates or empirical values for νS, νHCl, etc. The heat release rate is 

also dependent on the amount of oxygen and local temperature; that is combustion will only take 

place if there is sufficient oxygen and temperature for the reaction. Thus, unburned fuel may also 

be transported from the fire source and perhaps combusted in regions removed from the initial 

fire location. The level of detail in local burning is model dependent6

. 

 

5

 For example, the CFAST model [100] specifies combustion for most species relative to the production of carbon 

dioxide; the input for production of carbon monoxide is the mass of carbon monoxide produced relative to the mass 

of carbon dioxide produced. 

6

 In CFD fire models, combustion takes place within a single grid cell (control volume) dependent on the local 

conditions within the cell. In the simpler zone fire models, combustion is determined by the oxygen available in a 
52

4.2 Smoke and Species Transport 

Transport of mass and energy in computer fire models, including individual species, is simply 

based on a mass and energy balance at the boundaries. The level of detail naturally depends on 

the complexity of the model. For zone models, species transport, including soot, is tracked as it 

is generated by a fire, transports through vents from compartment to compartment, or mixed 

between layers (control volumes) within a compartment. For computational fluid dynamics 

(CFD) fire models, the transport is tracked from individual grid cells (control volumes) to 

adjacent cells. 

In either case, each unit mass of a species produced by a fire is carried in the flow to the control 

volumes and may accumulate within these. The model keeps track of the mass of each species in 

each volume, and knowing the volume of each control volume, one can easily calculate the 

concentration of each tracked species as a function of time. Detailed chemistry effects are not 

included, but are represented as a global representation. 

4.3 Modeling of Deposition on Compartment Surfaces 

Smoke deposition on compartment surfaces is an important phenomenon that needs to be 

understood to assess the effects of smoke far removed from the fire source. Both smoke 

particulates and gas phase species will deposit or stick to and react with compartment surfaces 

providing a sink to the fluid mass balance. A fairly accurate accounting of the smoke 

concentration at the location of critical electrical equipment vulnerable to failure is necessary to 

make a quantitative assessment. 

For hydrogen chloride, it has been shown [101,102] that significant amounts of the substance 

may be removed through adsorption by surfaces that contact smoke. HCl production is treated in 

a manner similar to other species. However, an additional term is required to allow for 

deposition on, and subsequent absorption into, material surfaces. Limited empirical data are 

available for deposition of HCl on several typical compartment surfaces that provide correlations 

for the adsorption and absorption of HCl. Data for other surfaces or acid gases is not available. 

FDS [103] includes a model for smoke deposition on bounding surfaces [104]. It is based on 

simplified thermophoresis and turbulent deposition mechanisms that exclude particle size effects. 

It has not been fully validated, but appears to improve the smoke concentration prediction 

somewhat [105]. 

4.4 Modeling of Equipment Damage 

Equipment damage from smoke stems primarily from an increased resistance in circuits and 

connections by corrosive metal loss, and creating conductive paths for current leakage due to 

smoke deposition. The former may take hours or days after the fire is extinguished to manifest 

 fire plume (in turn based on empirical correlations) or in a larger control volume within a compartment. Thus, 

oxygen-limited combustion is naturally a far more detailed process in a CFD model than in a zone fire model. 
53

itself in equipment failure, while the latter may occur at failure levels any time soon after initial 

smoke exposure. 

Though more typically based on laboratory measurement that compares the relative corrosion 

resistance of two or more materials, simple models for estimating the expected service life of 

components based on these laboratory measurements have been proposed [106,107]. Corrosion 

rates are expressed as an infinite series with the effect of environmental factors taken 

individually and in interaction. In many cases only a relatively small number of terms of this 

series would typically be required to make a prediction within the inherent uncertainty of the 

system. The laboratory measurements then look at the expected environment and the sensitivity 

of the rate in the expected mean environment to variations in each parameter to determine the 

coefficient for each term in the series. While the structure of the model has been defined, limited 

experimental data has been developed to date to support such a model. 

Tanaka et al. [6] have proposed a regression model to predict the degradation of surface 

insulation resistance based on smoke exposure tests. The regression model is not generic; it only 

applies to the fixed exposure time in the specific test apparatus described. It cannot be 

implemented in a fire model in a predictive manner where smoke concentrations, temperatures, 

humidity and flow fields are changing with time. Mangs, and Keski-Rahkonen [108] describe a 

model to predict insulation resistance deterioration based on the amount of smoke deposited, and 

ohmic conduction through the deposited soot. Hagen et al. [109] describe soot deposition on a 

probe consisting of parallel gold traces. The resistance behavior observed was non-ohmic and 

exhibited a critical loading consistent with percolation theory. 

Gallucci [110] has proposed a simplistic model to estimate the probability of damage to 

electronic devices based on potentially synergistic effects of exposure to smoke particles and/or 

elevated humidity. With data on smoke deposition from Tanaka et al. [6] and on probability of 

damage to electrical devices from Karydas [111], he developed a simple relationship between the 

probability, p, of damage and smoke concentration of 

݌ൌ1െ

1

݁஼்ିଷ ଵ଺ ⁄ (11)

where T is the smoke obscuration (m-1) and C is a constant taken to be 0.038 for vertical surfaces 

and 0.202 for horizontal surfaces. The effects of humidity are seen to accelerate the failure. The 

acceleration factor can be estimated from the temperature and humidity. A simple relationship is 

suggested as 

݇ ൌ 10

ఏାோுିଵ଺ହ

ସ଴ (12)

where θ is the temperature (°C) and RH is the humidity (%). The value of k is limited to the 

range of 1 to 1000. While its recommended use is for sensitivity or bounding analyses, it does 

include the important parameters of soot deposition, elevated temperature, and elevated 

humidity. All are seen as areas in need of additional experimentation and modeling. 

 

55

5 FUTURE RESEARCH NEEDS 

5.1 Smoke Production and Transport 

Butler and Mulholland give a very good synopsis of the generation and transport of smoke 

components [112]. They present the current state of knowledge about smoke aerosol phenomena 

that affect smoke toxicity: soot generation, fractal structure of soot, agglomerate transport via 

thermophoresis, sedimentation, diffusion, agglomerate growth through coagulation and 

condensation, and the potential of the aerosols to transport adsorbed or absorbed toxic gases or 

vapors into the lungs. The phenomena that affect smoke toxicity do or may play a role in the 

non-thermal damage of equipment due to smoke exposure except transport of absorbed or 

absorbed toxic gases or vapors into the lungs. The analog to transport of absorbed or adsorbed 

toxic gases or vapors into the lungs is transport of absorbed or adsorbed corrosive gases or 

vapors onto electrical conductors, so their discussions on absorption and adsorption are relevant 

here. They include tables of measured smoke yields and aerodynamic particle sizes, equations 

and references for the smoke agglomerate transport properties and wall loss. 

They conclude that the quality of fire hazard and risk assessment with regard to toxicants in 

smoke would be improved by conducting research in the following areas: 

 Measurement of mass median aerodynamic diameter of soot agglomerates avoiding 

 possible agglomerate structural changes with impactors. 

 Quantitative information on the adsorption of irritant gases on fire generated soot aerosol. 

 Quantitative information on the losses of toxicants to walls for a range of realistic fires. 

 Development of model for predicting smoke aerosol and vapor loss to the walls for a fire 

 in an enclosure. 

 Information on the size distribution of water droplets at fires, the conditions under which 

 they are formed, and the amount of gases adsorbed on the droplets. 

 Understanding the role of nanoparticles on the toxic effect of perfluoropolymer fumes. 

 

All but the last item would help facilitate or improve smoke transport fire modeling and the 

consequences of smoke exposures far from the fire room. 

The level of detail needed to describe smoke properties of interest depends on the effect of the 

smoke one wants to estimate. Light extinction can be estimated from the smoke concentration 

and the specific extinction coefficient [113] while particle size distribution, fractal structure, and 

optical properties are needed for predicting light scattering from soot [114]. It is not clear what 

the important smoke properties are, and the concentrations, or deposition conditions that 

significantly affect electrical or electronic equipment failure. 

At the moment, smoke generation is an empirical input for modeling purposes, with simple 

transport models and deposition models. Actually, smoke generation is a function of ventilation 

and thermal conditions for even pure materials. For complex fuels, combustion chemistry, gas 

chemistry, and liquid chemistry all contribute to products that arrive on and may react with 

electrical and electronic equipment. 
56

5.2 Modeling Smoke Deposition 

FDS [103] includes a simple model for smoke deposition to provide a gross estimate of smoke 

particle losses. It lacks detailed physics to describe particle mass loading on surfaces under 

specific conditions including gravitational settling. Typical forces acting on particles that may 

drive them to surfaces include diffusional forces (both Brownian motion and eddy diffusion), 

thermophoresis, inertial forces including gravitational settling, and electrical forces experienced 

by charged particles in electric fields and induced electrostatic forces between particles and nonconducting surfaces. In general, the dry deposition velocity characterizes the smoke mass 

deposition per unit area via the equation 

ܸ݀ݏ ൌ Flux

Concentration (13)

where Vds is the dry deposition velocity (m/s), Flux is mass flux to the surface (g/m2.s), and 

Concentration is the mass concentration (g/m3

). Thus, given a smoke mass concentration in the 

air next to a surface, the flux is the product of the concentration times the dry deposition 

velocity. Unfortunately, the dry deposition velocity is a function of all the forces acting on 

particles of a given size. Models have been proposed to estimate the dry deposition velocity of 

spherical particles of known size on semiconductor wafers [115,116]. Particles sized less than 

0.1 m in diameter fall into the diffusion-controlled deposition regime, where the deposition 

velocity increases with decreasing particle size. For vertically orientated surfaces, or horizontal 

face-down surfaces, the deposition velocity will continuously decrease as the particle size 

increases. For horizontal face-up surfaces, a minimum in the dry deposition velocity is observed 

at about 0.2 m to 0.3 m, and then it rises due to gravitational sedimentation, yielding a valleyshaped curve. A thermal gradient caused by a cooler surface than the surrounding fluid will 

increase the dry deposition velocity for all particle sizes, while a thermal gradient due to a hotter 

surface will decrease the dry deposition velocity for all particle sizes. 

In principle, if all details of particle size, and charge, air and surface temperature, flow fields, 

electric fields, and surface orientation are known, the dry deposition velocity as a function of 

particle size could be computed. If the aerosol concentration and size distribution are known, 

then the total flux to the surface could be calculated from summation of the contributions from 

each particle size. Typically though, the particle size distribution is not properly tracked in fire 

models, nor is there a detailed model of dry deposition velocity of agglomerate particles based on 

a representative agglomerate size. 

5.3 Prediction of Equipment Damage 

It is speculated that the main failure mechanisms for electrical and electronic equipment from 

smoke exposure during a fire in a NPP are due to circuit bridging from smoke deposits [6,25]. 

There is no absolute correspondence between the change in surface insulation resistance from 

smoke exposure and the failure of any electronic or electrical components. A relationship 

between surface insulation resistance from smoke deposition and the failure of real electronic 
57

circuits needs to be studied to establish correlations that could be used in probabilistic risk 

assessments. A smoke damage routine developed for a fire model could then assess the near 

term (during and soon after exposure) damage potential of electronics and electrical components 

due to smoke exposure. Fire models could provide inputs to a smoke damage estimates which 

would most likely include temperatures, humidity, flow fields, orientation, smoke concentration 

and properties. The smoke damage estimates could account the electronics or electrical 

component orientation, surface temperature, voltage potentials, and identified susceptibilities. 

The complexity and uncertainty and simplification of model inputs suggest a sub-model based on 

physics and empirical correlations for the predicted effects and the probability of equipment 

failure. 

 

59

6 CONCLUSIONS 

This report presents a review of smoke production measurement, prediction of smoke impact as 

part of computer-based fire modeling, and measurement and prediction of the impact of smoke 

through deposition of soot on and corrosion of electrical equipment. Equipment damage from 

smoke stems primarily from an increased resistance in circuits and connections by corrosive 

metal loss, and creating conductive paths for current leakage due to smoke deposition. The 

former may take hours or days after the fire is extinguished to manifest itself in equipment 

failure, while the latter may occur at failure levels any time soon after initial smoke exposure. 

The literature review on smoke corrosivity testing and damage due to smoke deposition 

emphasizes (despite extensive research on smoke corrositity) the lack of validated and widely 

applicable prescriptive or performance-based methods to assure electrical equipment 

survivability given exposure to fire smoke. Corrosion failures following smoke exposure take 

days or longer to manifest themselves, and corrective actions in the interim time can take place if 

the exposure is not too severe and intervention is timely. 

Circuit bridging via current leakage through deposited smoke was identified as an important 

mechanism of electronic and electrical equipment failure during NPP fires. In order to assess the 

potential for damage due to smoke exposure, relationships between smoke exposure and the 

failure of real electronic components need to be established. A smoke damage routine developed 

for a fire model could then assess the near term (during and soon after exposure) damage 

potential of electronics and electrical components design fire exposures. 

In the longer term, better understanding of combustion, gas-phase, and liquid chemistry could 

allow estimates of the formation rate of smoke and acid gases as a function of the ventilation, 

thermal, and fire environments. Understanding of absorption of acid gases by smoke and its 

deposition on surfaces (as a function of temperature, humidity, and smoke reactivity) would be 

necessary to develop models that could estimate the deposition behavior of smoke. 

61

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A-1 

APPENDIX A MATERIALS INCLUDED IN THE PFPC STUDY 

Table A-1. 25 Materials Included in the PFPC Study from Reference [72]. 

PFPC 

No. 

Company Product Designation Material Description 

1 BP EXP 839 XL olelin elstomer with metal hydrate filler 

2 Dow 5435-30-11 Blend of HDPE and chlorinated PE 

elastomer 

3 Dow 5348-40-1 Chlorinated PE with fillers 

4 Exxon EX-FR-100 EVA polyofefin with ATH filler 

5 GEP NORYL PX1766 Polyphenylene oxide/polystyrene blend 

6 GEP ULTEM 1000 Polyetherimide 

7 GEP SILTEM STM1500 Polyethermide/siloxane copolymer 

8 Himont Astryn AA36H Intumescent polypropylene 

9 Lonza Nylon with mineral filler 

10 UCC UNIGARD RE 

DFDA-1736NT 

XL polyolefin copolymer with mineral filler 

11 UCC UNIGARD RE 

HFDA-1393BK 

12 Quantum Petrothene XL 7403 

13 Quantum Petrothene YR 19535 

14 Quantum Petrothene YR 19543 

15 UCC UCARSIL FR7920NT 

16 BP Polycure 798 

17 Commercial sample 

18 Commercial sample 

19 Commercial sample 

20 Commercial sample 

21 UCC DGDK-3364NT 

22 Douglas fir 

23 Quantum Ultrathene UE 631 

24 Nylet P50 

25 UCC UNIGARD HP 

HFDA-6522NT 

 

B-1 

APPENDIX B EFFECT OF CORROSION PROBE THICKNESS 

In Part 4 [78] of the PFPC study, it is noted that for the cone corrosimeter that the amount of 

corrosion lost as measured by the 2500 Å probe was always higher than that measured by the 

45 000 Å probe for the same material. Since corrosion is a localized phenomenon, it is possible 

for different parts of a conductor to have different amounts of material removed. Considering the 

test probe as a series of resisters with different heights (due to local pitting) but the same width 

and length, the total resistance of the probe can be quite different than that of a probe of average 

thickness throughout. 

To show the impact of the thickness of the probe and the local variability of the corrosion, 

consider Figure B-1. It shows a range of probes with thicknesses from 2500 Å to 40 000 Å 

exposed to the same test environment. The “average loss” numbers are from the original data and 

are determined by calculation from total probe mass loss assuming mass is lost uniformly across 

the probes. 

Figure B-1. Modeled measures of metal loss (indicated by resistance change) with pitting. 

To estimate the impact of random pitting of a probe, a hypothetical probe was divided into a 

number of sections with the same width and height, but with a random variation in section height 

chosen such that the total mass lost was consistent with the average value. As can be seen the 

thicker the probe, the closer the average of the experiments matches the average mass loss 

calculation. For thinner probes, this results in individual sections particularly thin with higher 

resistance values. When the whole probe is considered as resistances in series, this results in a 

higher overall resistance. 

 

Probe Thickness (nm)

0 10000 20000 30000 40000

Loss Estimated from Resistance (nm)

1000

1200

1400

1600

1800

2000

2200

2400

Random Pitting

Half Error

Average Loss

C-1 

APPENDIX C ANALYSIS OF GAS COLLECTION IN A 

CORROSION TEST APPARATUS 

To extend the type of analysis of Gandhi [97,98] to consider the withdrawn ASTM E05 test, this 

section provides an idealized analysis of the gas volume within an arbitrary test chamber. The 

difficulty modeling the ASTM E05 test is the expansion bag, because that leads to a changing 

volume. Assuming an idealized expansion bag that keeps the pressure in the chamber constant 

leaves three state variables to describe the chamber: mass in chamber, M, the volume of the 

chamber V and the temperature in the chamber T. Because the chamber captures and holds all the 

effluent the change in mass can be described by 

mb dt

dm  (1)  (C-1)

where mb is the rate of the mass of the sample burning and  is the ratio of mass entrainment rate 

to mass burned rate as a function of height above the sample and the HRR of the sample,

  1 m  m en m b hcC . An energy balance can be used to calculate the temperature 





 



     

dt

dT T m

dt

dm

c mT c

dt

d

c m T

dt

dE

p b in p p (1 )  ( ) (C-2)

where E is the enthalpy in the chamber, cp is the heat capacity of air at constant pressure and Tin

is the temperature of the mass entering the chamber from the burning sample. Solving for rate of 

change of temperature yields 

( ) (1 ) T T

m

m

dt

dT in

b      (C-3)

Differentiating the volume using the ideal gas law gives 





 



   













  dt

dT T m

dt

dm

P

R

P

mRT

dt

d

dt

dV

0 0

ˆ ˆ (C-4)

where P0 is the constant pressure in the chamber and R  R M ave ˆ with R being the ideal gas 

constant and Mave is the average mass of a molecule of air. Notice that the rate of change in the 

volume is directly proportionally to the rate of change in the enthalpy in the chamber so that 

mbTin P

R

dt

dV (1 )  ˆ

0

  (C-5)

Calculating P0 in terms of initial conditions, making the substitution in the previous equation and 

grouping terms results in 
C-2 

0 0

0

0

0 0

(1 ) (1 ) ˆ

ˆ

T

T

m

m

m T V

V

m RT

R

dt

dV b in

b in

     

(C-6)

which interestingly enough is virtually the nondimensionalized differential equation for the 

volume. 

The three state equations that govern the gas collection system have now been defined. To 

understand the impact of a gas collection system on the corrosion test, it is important to look at 

factors that control corrosion, in this case the products produced by burning a test sample. 

Gandhi’s analysis focuses on the mass fraction, Ya, of a species a given that some fraction, ya, of 

the mass burned becomes a. While this assumption ignores details of any reaction chemistry, it is 

appropriate for a simple analysis of these gas collection systems. For the ASTM E05, test, 

consider what happens if a constant fraction of the mass burned, mb goes to producing a. That 

produces the following equation for the mass of a in the chamber, which can be written as M·Ys

with Ys being the mass fraction of a 

b a

a

a

a m y dt

dY Y m

dt

dm

dt

d mY     ( ) (C-7)

Solving for dYa/dt gives 





 



  

  a

a b a Y y

m

m

dt

d Y





1

( ) (1 )  (C-8)

Since corrosion is based on the concentration, which can be very different from the mass 

fraction, especially if the volume of the chamber changes, the change in concentration is given 

by 

2

( )

V

dt

dV V m

dt

d mY

V

mY

dt

d

dt

dC a

a



 



 



  (C-9)

Combining and simplifying gives 















  

  in

b a T

P

R C y

V

m

dt

dC

0

ˆ

1

(1 )



  (C-10)

Gandhi nondimensionalizes the equations using the initial conditions 

0

* m  m m (C-11)
C-3 

0

* V V V (C-12)

0

* T  T T (C-13)

b t  t (C-14)

b

b b t

m

m m* 0    (C-15)

*

0

* (1 ) (1 ) b

b b

f m

m

m t       (C-16)

to result in the following equations for the ASTM E05 gas collection system 

*

*

f d

dm  



(C-17)

* *

*

Tin f d

dV  



(C-18)

*

*

* * *

f

in

m

T T

d

dT    

(C-19)

*

*

1

f

a

a

a

m

Y y

d

dY 

   



(C-20)

*

*

* *

1

f

a

a

a

m

C y

d

dC 

   



(C-21)

According to the Annex of ASTM D 5485, the exposure chamber of the cone corrosimeter has a 

time constant of approximately 150 s. Another way of thinking about this is that with a specified 

flow of 4.5 L/min or 0.075 L/s if the gas in the exposure chamber (total volume of 11.2 L) is 

completely mixed then 0.075/11.2 = 0.007 of the effluent mass in the chamber is removed every 

second. With this, we can create a very simplified model of the amount of the effluent in the 

exposure chamber and what amount of the effluent came from which period of the combustion. 

We will assume that mixing is instantaneous and that there is no deposition. Obviously, there 

will be deposition but it is likely not to be a large fraction of the total effluent in the chamber. 

Using these assumptions, the amount of fire effluent in the chamber is 

mc mf 007mc    . (C-22)

Where mc is the mass of fire effluent in the exposure chamber and mf is the mass coming from 

the fire. 

The dependence of the concentration at any time ti during the burning phase of the test means 

that unlike the CNET test in ISO 11907-02, the final concentration is very dependent on the 

shape of the MLR during the test. Three different possible idealized mass loss curves are shown 
C-4 

in Figure C-1. Each burns for 600 s and has a peak HRR of 2 MW/m2

. The fraction of the mass 

flowing into the chamber that is product a is shown in Figure C-1. 

Figure C-1. Three possible mass loss curves as examples of idealized fires in an arbitrary 

corrosion test scenario. 

All three idealized fires lose a total of 600 g in 600 s during combustion. The difference is the 

time of the peak mass loss rate, which is 60 s for the fast fire, 240 s for the average fire and 420 s 

for the slow fire. Keeping with the standard that the exposure chamber is closed (the input and 

output from the exposure chamber closes) when 70 % of the mass has been lost in the fire gives 

shut down times of 288 s for the Fast fire, 345 s for the Average fire and 420 s for the Slow fire. 

Figure C-2 integrates the curves in Figure C-1 to yield the total mass in the exposure chamber 

versus time for the first 10 min the three fires. 

Time (s)

0 100 200 300 400 500 600 700

Mass Loss Rate (g/s)

-0.5

0.0

0.5

1.0

1.5

2.0

2.5

Fast 

Average 

Slow 
C-5 

Figure C-2. Total mass in exposure chamber for three idealized fires. 

Notice that the fast fire, which is shut down first, has the least mass in the exposure chamber 

while the slow fire has the most. To answer this question we take advantage of the simplicity of 

the model to note that the amount of mass that entered the exposure chamber at a particular time 

ti is dependent only on the difference between that time and the current time tc. This means we 

can determine how much of the total mass in the exposure chamber at the point where the 

chamber is closed off with the following equation 

( ) c i a t t

c f m m e    (C-23)

Where the function mc() returns the mass in the exposure chamber at the point the total mass lost 

reaches 70 % of the total mass that will be lost and tc is the time when the 70 % point is reached 

and a = -0.0067 gives the instantaneous rate that mass is being lost from the exposure chamber. 

The mass left in the exposure chamber for these three fires is given in Figure C-3. 

Time (s)

0 100 200 300 400 500 600

Total Mass Loss (g)

0

20

40

60

80

100

120

140

Fast

Average

Slow
C-6 

Figure C-3. Mass left in exposure chamber expressed as total mass and as a percentage of 

mass loss rate for three idealized fires. 

For all three fires the peak rate that mass is entering the chamber is 2 g/s. Less than a quarter of 

that mass is still in the chamber for the fast fire, half the mass is still in the chamber for the 

average fire but all of the mass is still in the chamber for the slow fire that is closed at the peak 

rate. Because so much time between when the peak amount of mass enters the chamber before 

the chamber closes in the fast fire, 228 s, there is more time for that mass to escape. In the slow 

fire, the peak amount enters the chamber and none of it is allowed to escape. Figure C-3 also 

shows the percentage of the total mass left in the exposure chamber is from each time period. 

One last question is would the shape of the MLR curve effect which material would be the most 

corrosive in the cone corrosimeter. Corrosion is a very dependent on local conditions and so is 

difficult to model on a large scale. However Tewarson [20] found that in his real scale tests 

corrosion scaled with the 0.6 power of concentration. So using that model and making the 

assumption that all the mass has the same level of corrosivity we can get an idea of the impact of 

shape on the total corrosivity. Figure C-4 shows the corrosivity calculated for the three fire 

sources. For the first 10 mins (inset), there is a noticeable difference in the three curves with the 

fast fire being the most corrosive and the slow fire the least. In the full hour of testing, the order 

changes. At the end of an hour the medium and slow fires are nominally identical and the fast 

fire is noticeable less corrosive. This suggests that shape of the mass loss curve can affect the 

overall corrosiveness of the material being tested. 

Time (s)

0 100 200 300 400 500 600

Mass In Chamber (g)

0.0

0.5

1.0

1.5

2.0

2.5

Mass In Chamber (%)

0.0

0.2

0.4

0.6

0.8

1.0

1.2

Fast 

Average 

Slow 
C-7 

Figure C-4. Estimated corrosive dose for three different idealized fire growth rates. 

 

Time (s)

0 1000 2000 3000 4000

Corrosive Dose ((g/L)2/3s)

0

2000

4000

6000

8000

10000

12000

14000

16000

18000

Fast 

Average 

Slow 

0 100 200 300 400 500 600

0

500

1000

1500

2000

D-1 

APPENDIX D CONDUCTIVITY AND CORROSION 

Typically, conductivity of combustion products is seen as an indicator of the potential for 

corrosion. The published data from the PFPC study [72,75-77] allows for more analysis to be 

performed. With test results from 24 materials it is possible to test if the strong correlation seen 

by Bottin [71] exists in these data. A plot of the conductivity as measured in DIN 57 472 against 

the results of CNET testing in Figure D-1 shows the relationship. 

While there is a clear correlation between conductivity and the increase in resistance in the 

CNET test, the correlation is different from the Bottin data with exponent of approximately 

7000 Siemens for the Bottin data being more than 30 times the PFPC exponent of approximately 

200 S. Still, the same functional relationship exists in both sets of data. 

In the CNET data, there is a group of materials with conductivity less than 250 S. Focusing on 

this data shows little correlation but the data does have bounds as can be seen in Figure D-2. 

DIN 57 472 Conductivity (S)

0.000 0.002 0.004 0.006 0.008 0.010 0.012

CNET Resistance (% increase)

0

10

20

30

40

50

60

y=4.485e223x

R2=0.74

Figure D-1. Comparison of CNET test results with conductivity as measured by DIN 

57 472. Data from reference [75,76]. 
D-2 

 

The resistance change is less than10 % and the conductivity is less than 250 S. This suggests 

that when an effluent that has low conductivity when dissolved in water, the material does not 

enhance the corrosion that occurs from the natural environment of a fire. 

Figure D-3 shows a similar comparison for the cone corrosimeter and the E05.21.71 test. For 

materials with conductivity greater than 900 S, the figure shows a correlation with the 

corrosimeter data though not as strong as the CNET data. Because the ASTM E05.21.70 test 

used a probe that was only 2,500 Å thick, values more corrosive materials all show values near 

2,500 Å. This indicates that all the material on the probe was corroded and thus no correlation is 

expected. The same lack of correlation exists for materials that have a particularly low 

conductance. 

DIN 57 472 Conductivity (S)

0 50 100 150 200 250

CNET Resistance (% increase)

0

2

4

6

8

10

12

Figure D-2. Comparison of CNET test results with conductivity as measured by 

DIN 57 472 for materials with conductivity less than 250 μS. Data from 

reference [75,76]. 
D-3 

Figure D-3. Comparison of cone corrosimeter and E05.21.71 test results with conductivity 

as measured by DIN 57 472. Data from reference [76,77]. 

Finally, we will consider how the CNET test results compare to the cone corrosimeter results. 

Figure D-4 shows a comparison the corrosimeter data against CNET data. The data breaks up 

into two groups with the upper group showing a reasonably linear correlation. The lower group is 

not well correlated but it is bounded and represents minor corrosion in both tests. If we just look 

at highly conductive materials, all the strongly correlated values of the upper group are included 

as well as one from the lower group. It is interesting to note that the pH value for this product, 

product 5.6, the highest pH of any of the high conductivity group. This correlation has been seen 

before by Gandhi [100] in his review of the data from the PFPC study, suggesting that pH has 

some role in predicting corrosion. 

To look at the relationship between pH and conductivity, it is reasonable to look at the same 

transform on the conductivity as is done to get the pH





 



   6 10 log c pS (D-1)

Figure D-5 shows the data with the high conductance and low conductance materials plotted as 

two different groups. 

Conductivity (S)

0 2000 4000 6000 8000 10000 12000

Material Loss (A)

0

1000

2000

3000

4000

5000

6000

Cone Corrosimeter

E05.21.71
D-4 

Figure D-4. Comparison of CNET test and cone corrosimeter test results for several 

materials. Data from reference [75,77]. 

Figure D-5. Comparison of acidity and conductivity for several materials from the PFPC 

Study. Data from reference [76]. 

CNET Resistance (% increase)

0 10 20 30

Cone CorrosimeterMaterial Lost (A)

0

1000

2000

3000

4000

5000

6000

All Data

Highly Conductive Materials

y=153x+983

R2

=0.75

pS

2345

pH

1

2

3

4

5

6

< 250 S

> 900 S

y = 0.703x + 0.494

R2

=0.91
D-5 

It is important to remember that the lower the number the higher the acidity or conductance. 

There is a trend in the data that linearly relates pH and pS with clearly some outlying data. 

Several of the polymer products have a component that is pH neutral but conductive given a 

relatively high pH but a lower conductance. So there is not necessarily a relationship between 

conductance and pH. Conductance being the driving force also answers the question of how 

bases can also be very corrosive. 

Even with 24 materials this is but a small sampling of possible materials. While the relationship 

between conductance and corrosion seems to be a strong one, it still warrants additional research. 

NRC FORM 335

(12-2010)

NRCMD3.7

U.S. NUCLEAR REGULATORY COMMISSION 1. REPORT NUMBER

(Assigned by NRC, Add Vol., Supp., Rev.,

and Addendum Numbers, if any.)

2. TITLE AND SUBTITLE

BIBLIOGRAPHIC DATA SHEET

(See instructions on the reverse) NUREG/CR-7123

3. DATE REPORT PUBLISHED

A Literature Review of the Effects of Smoke from a Fire on Electrical Equipment

MONTH

July I

YEAR

2012

5. AUTHOR(S)

R.D. Peacock, T.G. Cleary, P.A. Reneke, and D.C. Murphy

4. FIN OR GRANT NUMBER

N6761

6. TYPE OF REPORT

Technical

7. PERIOD COVERED (Inclusive Dates)

9/9/2009 - 7/30/2011

8. PERFORMING ORGANIZATION - NAME AND ADDRESS (If NRC, provide Division, Office or Region, U. S. Nuclear Regulatory Commission, and mailing address; if

contractor, provide name and mailing address.)

National Institute of Standards and Technology

Engineering Laboratory

100 Bureau Drive, Stop 8664

Gaithersburg, MD 20899-8664

9. SPONSORING ORGANIZATION - NAME AND ADDRESS (If NRC, type "Same as above", if contractor, provide NRC Division, Office or Region, U. S. Nuclear Regulatory

Commission, and mailing address.)

Division of Risk Analysis

Office of Nuclear Regulatory Research

U.S. Nuclear Regulatory Commission

Washington, DC 20555-0001

10. SUPPLEMENTARY NOTES

D.W. Stroup, NRC Project Manager

11. ABSTRACT (200 words or less)

A review is presented of the state of the art of smoke production measurement, prediction of smoke impact as part of computer-based

fire modeling, and measurement and prediction of the impact of smoke through deposition of soot on and corrosion of electrical

equipment. The literature review on smoke corrosivity testing and damage due to smoke deposition emphasizes (despite extensive

research on smoke corrosivity) the lack of validated and widely applicable prescriptive or performance based methods to assure

electrical equipment survivability given exposure to smoke from a fire. Circuit bridging via current leakage through deposited smoke

was identified as a potentially important mechanism of electronic and electrical equipment failure during nuclear power plant fires.

In the near term, assessment of potential damage can reasonably be based on the airborne smoke exposure concentration and the

exposure duration. Hence, models that can predict the airborne smoke concentration would be sufficient to provide upper limit

estimates of potential damage. In the longer term, it would be desirable to develop models that could estimate the deposition behavior

of smoke, and specifically correlate the combination of deposited and airborne smoke to component damage.

12. KEY WORDS/DESCRIPTORS (List words or phrases that will assist researchers in locating the report.)

corrosivity, electrical equipment, equipment damage, literature review, smoke movement, smoke

transport

NRC FORM 335 (12-2010)

13. AVAILABILITY STATEMENT

unlimited

14. SECURITY CLASSIFICATION

(This Page)

unclassified

(This Report)

unclassified

15. NUMBER OF PAGES

16. PRICE


UNITED STATES 

NUCLEAR REGULATORY COMMISSION

WASHINGTON, DC 20555-0001

--------------------

OFFICIAL BUSINESS
NUREG/CR-7123 A Literature Review of the Effects of Smoke from a Fire on Electrical Equipment