Patent Publication Number: US-2015086930-A1

Title: System and method for retrofitting a burner front and injecting a second fuel into a utility furnace

Description:
CROSS-REFERENCE TO RELATED APPLICATIONS 
     This application is a continuation of and claims priority to International Application No. PCT/US2013/044296, filed Jun. 5, 2013, and entitled SYSTEM AND METHOD FOR RETROFITTING A BURNER FRONT AND INJECTING A SECOND FUEL INTO A UTILITY FURNACE, which is a continuation-in-part of and claims priority to U.S. application Ser. No. 13/492,479, filed Jun. 8, 2012, and entitled SYSTEM AND METHOD FOR INJECTING COMPOUND INTO UTILITY FURNACE, which is a continuation-in-part of and claims priority to International Application No. PCT/US2010/059886, filed Dec. 10, 2010, and entitled SYSTEM AND METHOD FOR INJECTING COMPOUND INTO UTILITY FURNACE, which designates the United States and is itself a PCT continuation-in-part of and claims priority to U.S. application Ser. No. 12/636,446, filed Dec. 11, 2009, and entitled SYSTEM AND METHOD FOR INJECTING COMPOUND INTO UTILITY FURNACE, all of which are incorporated herein by reference in their entirety. 
    
    
     FIELD OF INVENTION 
     The subject of this disclosure may relate generally to systems, devices, and methods for facilitating the injection of various compounds, including liquid and gas fuels, into a utility furnace. 
     BACKGROUND OF THE INVENTION 
     Utility furnaces are used in various industries for a variety of different purposes. Common issues associated between these various industries include the handling of the byproducts created by the combusted fuel. These byproducts can decrease the utility furnace efficiency and pose other pollution problems 
     In one example, the pulverized coal, used in various types of boilers, burns in a combustion chamber. The hot gaseous combustion products then follow various paths, giving up their heat to steam, water and combustion air before exhausting through a stack. The boiler is constructed mainly of interconnected elements such as cylinders such as the super heater tubes, water walls, various larger diameter headers, and large drums. Water and steam circulate in these elements, often by natural convection, the steam finally collecting in the upper drum, where it is drawn off for use. Water/steam tubes typically almost completely cover the walls of the passage so that they efficiently transfer heat to the water/steam. As the coal is burned, ash and/or other products of combustion build-up on the tubes. 
     Presently sootblowers are available to aid in the removal of these build-ups. Soot-blowers are mechanical devices used for on-line cleaning of ash and slag deposits on a periodic basis. They direct a pressurized fluid through nozzles into the soot or ash accumulated on the heat transfer surface of boilers to remove the deposits and maintain the heat transfer efficiency. The soot and dust generated in combustion get deposited on outer tube surfaces. This adds to the fuel requirements to maintain heat transfer into the water/steam heated by the utility furnace. Running with added fuel in turn increases deposition of byproducts of fuel burning and also increases the chances of the tubes failure by overheating. This eventually results in shutting down of the furnace for repairs. All this can be avoided by soot blowing. Regular soot blowing saves fuel and boiler downtime. In other words steam at constant parameters is available over a longer period of time. Numerous types of sootblowers exist including but not limited to wall sootblower, long retractable sootblower, rotating element sootblower, helical sootblower, and Rake-type blower. Under optimal conditions this ash is removed from the surface of the tubes by pressured fluid (typically air, saturated steam or super-heated steam) delivered from sootblowers. However under suboptimal conditions the ash melts due to reaching its fusion temperature and results in the formation of slag. Sootblowers are less effective at removing the slag. 
     The major problem with the formation of slag is that it insulates the elements, thus requiring the furnace to burn at a hotter temperature to create the same increase in water temperature. Excessive ash deposits on a coal-fired boiler&#39;s heat transfer surfaces will reduce its efficiency, and in extreme cases a boiler can be shut down by ash-related problems. Slagging incidents are a heavy drag on the global utility industry due to reduced power generation and equipment maintenance. 
     The changing electricity market and political pressures have pushed the use of fuels other than coal. For example, use of gas, biofuel, cofired fuel, etc. has become widespread. These factors have led to coal-fired plants being operated under unusual loads. This change in operation has altered the effects of boiler slagging. The cofiring of other fuels with coal, especially biomass, represents a large challenge to utility furnace operation. The ash chemistry of these alternative fuels is often very different to that of the coals and has given rise to serious problems. The tendency of coal for slagging depends on its composition. The complex interaction between a boiler&#39;s operating conditions and the fuel chemistry makes the prediction of slagging difficult. Furthermore, the increasing pressure on coal-fired power stations to reduce emissions has led to the development of technologies for the abatement of specific pollutants that impact on ash slagging. The new generation of pulverized coal fired plant, designed for high efficiency through the use of high steam temperatures and pressures, present further challenges with respect to ash slagging and fouling. 
     Various methods of removing the slag other than with a sootblower are in use. For example in some power plants, engineers fire shotguns into the furnace to break the slag off of the pipes. Other methods require taking the furnace off line to deal with the problem. Other methods include a specialized system that is located to access flue gasses whereby the system uses a specialized pressure source (i.e., different from that used by the facility for the operation of the sootblowers) to force a fluid into a feed tube, which mixes the fluid with a chemical coming from atomizing nozzles. The fluid and chemical is then injected into the flue gas stream which may allow incidental contact with areas affected by slagging. However, this method requires enormous amounts of chemical to be dumped into the flue gas stream which is difficult if not impossible to understand as the flow dynamics in the furnace are constantly changing. For example, the buildup of slag between tubes redirects the flue gas away from those tubes preventing the slag from receiving the chemical. Furthermore, the specialized equipment and the special access for introducing the chemicals from a specialized system into the utility furnace substantially increases cost. Thus, these techniques are less than satisfactory. 
     In dealing with the byproducts released into the environment (pollution), various systems associated with the utility furnaces process the byproducts before their release. However, better methods of chemical processing of these byproducts are constantly sought after. New utility furnaces are almost certain to be required to operate under conditions that facilitate carbon capture and storage, for compliance with climate change driven requirements. While such requirements are frequently sought in relation to coal fired furnaces they could also apply to a variety of fuel types. 
     While the problems and limitations of utility furnaces are clear, there are few solutions. The presence of certain compounds in the utility furnaces have been experimented with and resulted in improved abilities to deal with slag and pollution. While the specific compounds vary across the board depending on the specific chemistry of the fuel and problem to be addressed, one uniform problem exists, there is no adequate delivery mechanism to inject the compounds into targeted spots in the furnace. 
     A solution to the problem of delivering various compounds to targeted locations of a utility furnace is needed. As such a solution to the delivery of compounds into a utility furnace is presented herein. 
     SUMMARY OF THE INVENTION 
     In an example embodiment, an apparatus comprises: a mixing chamber configured to receive a compound operable to improve at least one of harmful emissions and slagging in a utility furnace. In this embodiment, the mixing chamber is further configured to mix the compound with a fluid to be injected into the utility furnace, and the fluid is delivered by a fluid supply which is in place at the utility furnace. 
     In an example embodiment, a method comprises: attaching a compound feed to a mixing chamber connected inline with a fluid supply; supplying the compound to the mixing chamber; mixing the compound with a fluid; and delivering the compound and the fluid to a utility furnace. 
     In an example embodiment, a system comprises: a fluid supply delivering a fluid under pressure for use at a utility furnace; a compound capable of improving efficiency of the utility furnace; a mixing chamber operable to combine the fluid under pressure with the compound, wherein the mixing chamber is configured to be removably connected to the fluid supply; and a mechanism connected to the fluid supply that directs the fluid under pressure into the utility furnace. 
     In an example embodiment, a method of retrofitting a utility furnace is provided. In this method, the utility furnace has a burner front, the burner front fires the utility furnace with a first fuel type, and the burner front supplies combustion air associated with the combustion of the first fuel type, and the combustion air comprises at least one of: primary air, secondary air, and tertiary air. The method comprises: connecting a source of a second fuel type to the burner front, wherein the connection is configured to introduce the second fuel type into the combustion air; wherein the first fuel type is a different type of fuel from the second fuel type. 
     In an example embodiment, a method of injecting a compound into a utility furnace comprises: injecting a compound into a preexisting fluid stream; wherein the preexisting fluid stream is a fluid stream carried in an already existing conveyance device, wherein the already existing conveyance device was connected to the utility furnace, in such a manner as to inject the preexisting fluid stream into the utility furnace, prior to retrofitting the utility furnace to provide the ability to inject the compound into the fluid stream; injecting the preexisting fluid stream, containing the compound, into the utility furnace through one of a burner front and a sootblower. In this example method, the compound comprises one of: a solid, a liquid, and a gas. 
     In an example embodiment, a method of injecting a compound into a utility furnace comprises: delivering a compound into the utility furnace by injecting the compound into a delivery mechanism conveying a combustion air, wherein the combustion air is one of primary air, secondary air, and tertiary air, wherein the compound comprises a fuel that is not a primary fuel for firing the utility furnace. 
     In an example embodiment, a utility furnace comprises: a burner; a delivery mechanism, wherein the delivery mechanism is configured to deliver combustion air into the utility furnace, wherein the delivery mechanism is configured to deliver combustion air into the utility furnace in the vicinity of the burner, wherein the combustion air comprises one of primary air, secondary air and tertiary air; a fuel source provided to the burner, wherein the fuel source is a first fuel type and is the primary source of fuel to the utility furnace; and a compound source, connected to the delivery mechanism, wherein the compound source is configured to supply the compound into the combustion air in the delivery mechanism. 
     In accordance with various aspects of the present invention an apparatus comprises a mixing chamber configured to receive a compound for improving environmental and/or efficiency conditions in a utility furnace, wherein the mixing chamber is further configured to mix the compound with a fluid which is in a pressurized fluid system in place with the utility furnace and configured to inject the fluid and compound into a utility furnace. 
     In another exemplary embodiment, a system comprises a fluid supply configured to deliver a fluid; a valve connected to the fluid supply wherein the valve is operable to control the fluid from the fluid supply; a feed tube configured to connect to the valve and transport the fluid; a delivery device configured to connect to the feed tube and configured to eject the fluid into a utility furnace; a compound capable of improving the efficiency of the utility furnace; a hopper configured to hold a quantity of the compound; an delivery system connected to the hopper and operable to transfer compound from the hopper; and a mixing chamber operable to receive the compound from the delivery system and combine the compound with the fluid supply wherein, the mixing chamber is configured to be removably connected to the valve. 
     In another exemplary embodiment, a system comprises a fluid supply configured to deliver a fluid; a valve connected to the fluid supply wherein the valve is operable to control the fluid from the fluid supply; a delivery system configured to connect to the fluid supply; a compound capable of improving the efficiency of the utility furnace; a mixing chamber operable to receive the compound from the delivery system and combine the compound with the fluid supply; the mixing chamber located in line with the fluid supply; the fluid supply delivering a mixture of fluid and compound to the air blowers of a burner, the air blowers connected in line to the fluid supply configured to inject the mixture into the furnace. 
     Furthermore, in an exemplary embodiment a method comprises attaching a mixing chamber inline with a fluid supply; delivering a compound to the mixing chamber mixing the compound with the fluid supply forming a mixture; delivering the mixture to a utility furnace through a manufactured sootblower; covering areas of the furnace accessible by sootblowers; and impregnating the compound to affected slagging areas regardless of changing flue gas flow dynamics. 
     Furthermore, in an exemplary embodiment a method comprises attaching a mixing chamber inline with a fluid supply; delivering a compound to the mixing chamber mixing the compound with the fluid supply forming a mixture; delivering the mixture to a utility furnace through a burner; covering areas of the furnace accessible by the furnace; and impregnating the compound to affected slagging areas. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
       These and other features, aspects, and advantages will become better understood with reference to the following description, claims and accompanying drawings where: 
         FIG. 1  is an exemplary utility furnace depicting sootblower locations; 
         FIG. 2   a  is an exemplary retractable sootblower and an example of distribution from the retractable sootblower; 
         FIG. 2   b  is an exemplary wall mounted sootblower and an example of distribution from the wall mounted sootblower; 
         FIG. 2   c  is an exemplary wall mounted sootblower and an example of distribution from the wall mounted sootblower; 
         FIG. 2   d  is another exemplary wall mounted sootblower and an example of distribution from the wall mounted sootblower; 
         FIG. 2   e  is an exemplary array of wall mounted sootblowers and an example of distribution from the array of wall mounted sootblower; 
         FIG. 3  is an exemplary embodiment of a flow process of a system for injecting compound into a utility furnace; 
         FIG. 4   a  is a cross section of an exemplary embodiment of a nozzle used to mix various compounds and pressurized fluid; 
         FIG. 4   b  is a cross section of an exemplary embodiment of a mixing chamber used to mix various compounds and pressurized fluid; 
         FIG. 5   a  is cross section of an exemplary embodiment of an apparatus for mixing a compound with a pressurized fluid; 
         FIG. 5   b  is cross section of an exemplary embodiment of an apparatus for mixing a compound with a pressurized fluid; 
         FIG. 6  is an exemplary embodiment of distribution of a compound from a wall mounted sootblower; 
         FIG. 7  is an exemplary embodiment of distribution of a compound from a retractable sootblower; 
         FIG. 8   a  is an exemplary embodiment of a system delivering compound into air to a burner; 
         FIG. 8   b  is an exemplary embodiment of a burner receiving compound through secondary air; 
         FIG. 9  is an exemplary embodiment of a method of the present invention; and 
         FIG. 10  is an exemplary embodiment of a burner front configured to receive a second fuel source in the combustion air near the exit of the primary fuel source from the burner. 
     
    
    
     DETAILED DESCRIPTION 
     In accordance with an exemplary embodiment of the present invention, systems, devices, and methods are provided, for among other things, facilitating the injection of various compounds into a utility furnace. The following descriptions are not intended as a limitation on the use or applicability of the invention, but instead, are provided merely to enable a full and complete description of exemplary embodiments. 
     In accordance with various exemplary embodiments of the present invention, a compound may be injected into a utility furnace by mixing with a pressurized fluid going into the utility furnace. In various examples the compound may be merely injected under pressure into the pressurized fluid. In various embodiments the system may be configured to pull the compound into the fluid. These examples may be combined as well. As will be discussed herein the terms nozzles and/or mixing chambers may be used to describe the devices, locations and situations in which compound and the pressurized fluid are mixed. While each term may be discussed in various examples and embodiments it is noted that either term may be used without excluding the other from application in the examples and embodiments. 
     In accordance with an exemplary embodiment, with reference to  FIG. 4   a , nozzle  400   a  may have a first side  404   a , an inlet side to the fluid, and a second side  402   a , an exit side to the fluid. Nozzle  400   a  may be variously sized to accommodate the equipment that it mates to. In one exemplary embodiment nozzle  400   a  may be approximately 1-3 inches in diameter at the outlet to accommodate common feed tube sizes used with utility furnaces. However, nozzle  400   a  can be sized to fit various components. In accordance with one embodiment, nozzle  400   a  may have a varying cross-section between the first side and the second side. In various embodiments, the varying cross-section of the nozzle may comprise a long radius  412   a . The long radius may have its largest opening in the nozzle on first side  404   a  and the smallest diameter cross-section on second side  402   a . In accordance with an exemplary embodiment, nozzle  400   a  comprises a varying cross section that causes a high pressure on first side  404   a  relative to a low pressure on the second side  402   a.    
     The nozzle may also have a compound entrance  408 . In an exemplary embodiment, the compound may be brought into nozzle  400   a  via compound entrance  408 . Nozzle  400   a  may also have a compound exit (also referred to herein as chemical injection port). In an exemplary embodiment the compound exits nozzle  400   a  via compound exit  406   a . In accordance with an exemplary embodiment of the present invention, nozzle  400   a  may be configured for mixing a compound with a pressurized fluid stream. 
     In accordance with various embodiments, nozzle  400   a  may be merely a mixing chamber. For example, nozzle  400   a  may be configured for mixing a compound with a pressurized fluid stream. This mixing occurs in response to the compound coming into contact with the fluid being carried within the fluid supply.  FIG. 4   a  is illustrative of this in that the cavity into which the compound exits, at the compound exit  406   a , is the same cavity into which the pressurized fluid exits at the second side  402   a , and thus forms a mixing chamber. The radius/varying cross section  412   a  is beneficial in creating a condition in the system that draws the compound into the mixing chamber. As such, all nozzles may be mixing chambers but all mixing chambers may not be nozzles. 
     In accordance with various embodiments, a mixing chamber may be employed to mix a compound and a pressurized fluid stream. With reference to  FIG. 4   b , mixing chamber  400   b  may have a first side  404   b , an inlet side to the fluid, and a second side  402   b , an exit side to the fluid. Mixing chamber  400   b  may be variously sized to accommodate the equipment that it mates to. In one exemplary embodiment mixing chamber  400   b  may be approximately 1-3 inches in diameter at the outlet to accommodate common feed tube sizes used with utility furnaces. However, mixing chamber  400   b  may be sized to fit various components. 
     The mixing chamber may also have a compound entrance  408 . In an exemplary embodiment, the compound may be brought into mixing chamber  400   b  via compound entrance  408 . Mixing chamber  400   b  may also have a compound exit  406   b  (also referred to herein as chemical injection port). In an exemplary embodiment the compound exits mixing chamber  400   b  via compound exit  406   b . In accordance with an exemplary embodiment of the present invention, mixing chamber  400   b  may be configured for mixing a compound with a pressurized fluid stream. 
     In various embodiments, a mixing chamber may comprise a point where a compound supply line and a fluid supply line intersect. In one example a mixing chamber may be a distinct separate part added to a fluid supply line. For example, mixing chamber  400   b  may be added in-line. In another example, a fluid supply line may be tapped into directly with a second line. Compound may be delivered under pressure through the second line into the fluid supply line. In this embodiment, the mixing chamber may be the point or region of the system where the pressurized fluid and the compound intersect. Any of variety of fluid supply lines on a utility furnace may be accessible for incorporating a mixing chamber, including plant instrument air, service air, primary air into the furnace, secondary air into the furnace, and/or tertiary air into the furnace. The fluid may further comprise steam or various pressurized water sources. 
     In an example embodiment, the fluid medium used in the sootblowers is air, and the compound added is just water. The water, in this example, can flash to steam and has proven effective in sootblowing in this fashion. Thus, the mixing chamber facilitates retrofitting a sootblower to be able to meter an amount of water into the sootblower air stream. 
     In various embodiments of the present invention, the nozzle may further comprise a valve  410 . One exemplary embodiment, valve  410  may be a ball valve. In another exemplary embodiment, valve  410  may be a gate valve. Valve  410  may control the flow of the compound. In accordance with various embodiments of the present invention, the flow of the incoming compound may be stopped and started by opening and closing valve  410 . In other exemplary embodiments, valve  410  may prevent the compound from flowing away from nozzle  400   a  and only allow the compound to flow into nozzle  400   a . For example, valve  410  may be a check valve. 
     In accordance with an exemplary embodiment of the present invention, an apparatus for mixing a compound with a pressurized fluid stream comprises a mixing chamber, a valve, and a feed tube. In this embodiment, referring to  FIG. 5   a  and/or  FIG. 5   b , nozzle  500   a  and/or mixing chamber  500   b  may be positioned between valve  506  and feed tube  504 . The pressurized fluid can pass through nozzle/mixing chamber  500   a /b coming from valve  506  and flowing into feed tube  504 . Furthermore, nozzle/mixing chamber  500   a /b may be configured to receive the compound at entrance  508  and mix the compound with the pressurized fluid stream. 
     In various exemplary embodiments nozzle/mixing chamber  500   a /b may include features which allow for the connection of nozzle/mixing chamber  500   a /b to valve  506  or to feed tube  504 . Such features might include any of a variety of fasteners known in the industry e.g., bolts, weld, pressure fittings, bracketed flanges, etc. In other various embodiments nozzle/mixing chamber  500   a /b may be an integral or integrated part of valve  506  or feed tube  504 . For example, nozzle/mixing chamber  500   a /b and feed tube  504  may be manufactured as one piece. In an alternate example valve  506  and nozzle/mixing chamber  500   a /b may be manufactured as one piece. Likewise, all three elements may be manufactured as one piece. 
     In one exemplary embodiment, valve  506  is a poppet valve. In other embodiments valve  506  is any of a variety of valves include but not limited to diaphragm valves, pressure regulator valves, check valves, etc. In various embodiments of the present invention valve  506  can be any of a variety of valves used in the art whereby the valve controls the flow of fluid. Furthermore, valve  506  may be configured to adjust the pressure of the fluid passing through. 
     As discussed above, the apparatus may further comprise feed tube  504 . In various embodiments of the present invention, feed tube  504  may be configured to attach directly to either valve  506  or nozzle/mixing chamber  500   a /b. In an exemplary embodiment feed tube  504  may be configured to be detached from valve  506  and attached to nozzle/mixing chamber  500   a  or  500   b  inserted between feed tube  504  and valve  506 . In this manner, an existing device may be retrofitted to include the nozzle/mixing chamber  500   a /b. As discussed above the feed tube may also be integrated with nozzle/mixing chamber  500   a /b and/or valve  506 . In various embodiments, feed tube  504  may be configured to withstand the pressure and corrosion caused by any material flowing through it. In various examples, fluid may flow through the feed tube at 300 SCFM to 1000 SCFM. However, depending on the application smaller or larger rates may be used. The feed tube may be comprised of hardened steel that is capable of withstanding the mixture of the high pressure fluid and also the compound introduced at nozzle/mixing chamber  500   a /b. Further, other various materials may be used depending on the intended use of the system. In some instances the feed tube may be a component already installed in a facility incorporating the apparatus. 
     In one exemplary embodiment of the present invention, the compound introduced at nozzle/mixing chamber  500   a /b may be any of a variety of solids, liquids, or gases that may beneficially be injected into a utility furnace. Furthermore, the compounds should be configured such that they are capable of being transported in line through a pressure system. In various examples the compound may be caused to move through the system via a positive pressure or a negative pressure. 
     In accordance with an exemplary embodiment, a compound in solid form may be sufficiently granular that it can pass through various types of tubing. In one exemplary embodiment, the compound may be a solid agent or a dry compound, being a substantially dry, granular solid having insignificant levels of humidity or liquid. In various exemplary embodiments, the compound is delivered as a slurry, liquid, or gas. For example, delivering the compound as a slurry, liquid, or gas may be beneficial where pumping is incorporated. This may be especially true where there are high pressures to overcome at the nozzle. In another example, delivering the compound as a solid may be beneficial when the compound is delivered by transport air created by a vacuum. Various examples of compounds used in the system may include, but are not limited to, magnesium hydroxide, potassium hydroxide, sodium hydroxide, aluminum hydroxide, hydrogen peroxide, magnesium, kaolin, mullite, trona, sodium bromide, potassium bromide, magnesium carbonate, magnesite, micronized limestone, urea-based solids delivered dry or wet, and/or ammonia. Any such compound that may be desirable for a variety of chemically reactive, cleaning, processing or other beneficial purposes inside of a utility furnace may also be incorporated. Thus, in an example embodiment, where the compound is for example ammonia or urea-based, the injection of the compound may facilitate selective non-catalytic reduction in the furnace or the backend flue gas. 
     In one exemplary embodiment of the present invention, the fluid comprises pressurized air. In other various embodiments the fluid might comprise steam. Moreover, the fluid may comprise any compressed or pressurized fluid capable of being injected into the system. 
     In accordance with an exemplary embodiment of the present invention, the apparatus for mixing a compound with a pressurized fluid stream (comprising a nozzle, a valve, and a feed tube) may be used or adapted to a utility furnace. In an exemplary embodiment, and with reference to  FIG. 3 , the apparatus may also be incorporated into a larger system wherein the system comprises compound feed mechanism  300  which comprises compound  302 , compound storage  304 , and mixing chamber  306 , coupled inline with fluid delivery system  320  which comprises fluid supply  322 , valve  324 , feed tube  326  and delivery mechanism  328  either removably or permanently coupled to utility furnace  330 . 
     The fluid, as contemplated in an exemplary embodiment of the system, may comprise any of a steam, air or other compressed gasses or fluids typically released in a utility furnace. In accordance with an exemplary embodiment the fluid supply may be an air compressor, steam recirculation system, pump, pressure vessel etc. Furthermore, the fluid supply may be any commercially available mechanism capable of creating, maintaining, or adjusting these pressures as contemplated herein. The fluid supply may be positioned and/or coupled to valve  324  directly or by means of other connections and/or devices. 
     In accordance with an exemplary embodiment of the present invention, referring to  FIG. 7 , the delivery mechanism may be lance  718  and/or injection nozzle  720 . In another exemplary embodiment, the delivery mechanism comprises the injection nozzle associated with a wall blower. In various exemplary embodiments, the delivery mechanism may be any permanent or temporary fixture on the utility furnace. In various exemplary embodiments of the present invention, a delivery mechanism is any component capable of delivering the pressurized fluid and/or fluid mixed with compound into a utility furnace. 
     In one exemplary embodiment, lance  718  may be capable of being inserted partially or fully into a utility furnace. The lance tube is what is carried and rotated into the furnace by a gearbox/motor attached to the sootblower. The lance tube may surround the stationary feed tube and is sealed by a gland. In another exemplary embodiment, injection nozzle  720  is configured to deliver the fluid supply and/or the fluid supply compound mixture to specific locations inside the utility furnace, such as to a wall as depicted in  FIG. 2   b  or out into an open chamber as depicted in  FIGS. 2   a ,  2   c ,  2   d  and  2   e . Thus, the compound can be delivered to the exhaust gas, exhaust chamber, combustion chamber, pre-combustion (e.g., burner), water walls, pipes, superheat tubes, the back pass, or any other element in a utility furnace or its exhaust gas stream. 
     With reference to the compound, as discussed above, the compound may be received by the nozzle. This compound may be stored in any of a variety devices connected to the nozzle. In accordance with an exemplary embodiment, and with reference to  FIG. 6 , a compound storage device  614  may comprise a hopper with an auger feeder connected either directly or indirectly to nozzle  602 . In one example, the compound is stored in a non-pressurized hopper. In one example, the hopper may store a wet compound. In another example, the hopper may store a dry compound. In accordance with various other exemplary embodiments, compound storage device  614  may comprise a storage container and pressure mechanism. In such an embodiment, the compound may be stored and delivered by the pressure mechanism which may include pressurized vessels, gravity feed, pumps (including any of a variety of direct lift, positive displacement, velocity, buoyancy, centrifugal and/or gravity pumps), conveyors or any commonly known apparatus capable of delivering the compound to the inlet of the nozzle. For example, the pressure mechanism may comprise positive displacement pump  618 . Pump  618  may be located with storage device  614 . Pump  618  may also be located along delivery line  610 , providing pressure to nozzle and or mixing chamber  602 . Pump  618  may delivery a wet compound to nozzle and or mixing chamber  602 . 
     Various quantities of this compound may be incorporated in the use and functionality of the system herein discussed. In one exemplary embodiment, upwards of 1000 lbs of compound per cleaning cycle may be injected into a utility furnace for the removal of soot. However, the quantities can vary depending on the size of the utility furnace and purpose for which the compound is being injected. 
     While the compound can be delivered and/or received by the mixing chamber/nozzle in a variety of ways as discussed previously, the motivation of compound through the mixing chamber/nozzle can also occur in a variety of ways. In accordance with an exemplary embodiment of the present invention, a vacuum may be present on the second side of nozzle  400   a  which may create a force which may draw sufficient amounts of compound into the fluid stream to be delivered with the system. In one exemplary embodiment, nozzle  400   a  may cause 60 inches of vacuum (i.e., a drop in pressure expressed in inches of water). In various other embodiments the vacuum can be greater or less than 60 inches of water depending on the application. For example, there can be no vacuum at nozzle  400   a  but instead nozzle  400   a  may create a zone of static or low pressure compared to the fluids in the sootblower. Variations on the profile of the nozzle can be optimized to produce a sufficient vacuum and/or a maximum pressure drop. In other various embodiments, the compound may be pressurized by a pump or the like and introduced into the fluid stream under pressure. Such pressurization can occur in any way typical of the art including, but not limited to the forces created by the devices discussed above. 
     Referring again to  FIG. 3 , and in an exemplary embodiment, fluid delivery mechanism  320  as discussed above can be configured to deliver a pressurized fluid flow into utility furnace  330 . In one exemplary embodiment, the utility furnace is a coal fired induction draft power plant furnace. Moreover, a utility furnace may be any of a commercially available or custom furnaces including but not limited to boilers, HVAC, cokers, pulp and paper furnaces, etc. In an exemplary embodiment the furnace may be any of a variety of boilers fired by a variety of fossil fuels including, but not limited to, coal, petroleum, natural gas, etc. In other various embodiments of the present invention, a utility furnace might include any of a variety of boilers fired by alternative fuels, such as, for example, bio fuels or a combination of bio fuels and fossil fuels. In various exemplary embodiments of the present invention, utility furnace  320  may comprise furnaces used in a variety of industries including metal refineries, (e.g., cokers), pulp and paper, energy production, waste disposal, heating, etc. 
     Referring to  FIG. 1 , sootblowers can be located in numerous locations around a furnace. Variations in numbers and locations depend on the size and type of furnaces. Each location may be specifically targeted to allow access to particular elements or locations inside of the furnace. In an exemplary embodiment, these strategically located sootblowers can be used to deliver compound into the furnace. For example, wall mounted sootblowers may be located in the primary combustion area of the furnace. Also, retractable long lance type sootblowers may be located in the superheater or back pass portions of the furnace. In accordance with various other exemplary embodiments, a utility furnace may have various types of sootblowers located near superheaters, reheaters, convection section of horizontal tubes, the economizer and/or air preheaters. Furthermore, in various embodiments, compound injection may be used via pressurized fluid stream at any sootblower location. 
     In an exemplary embodiment of the present invention, and with reference to  FIG. 6 , a coal fired furnace system may comprise wall mounted sootblowers  616 . Wall mounted sootblower  616  may, for example be a Diamond Power Model IR-3Z sootblower or a Clyde Bergemann Model RW5E. Furthermore, wall mounted sootblower  616  may comprise any device configured to deliver fluid to the interior walls of a utility furnace. 
     In an exemplary embodiment, wall mounted sootblower  616  may comprise feed tube  604  and valve  606 . In one exemplary embodiment nozzle  602  is inserted between feed tube  604  and valve  606 . For example nozzle  602  may be retrofitted into wall mounted sootblower  616 . In another example, wall mounted sootblower  616  may be originally constructed with nozzle  602  between feed tube  604  and valve  606 . In various exemplary embodiments, nozzle  602  may be a component of a compound feed mechanism  600  which comprises valve  608 , feed line  610 , transport air valve  612  and compound storage  614 . Valve  608  may be coupled to feed line  610 . Feed line  610  may be coupled to transport air valve  612 . Transport air valve  612  may be coupled to compound storage  614 . 
     In an exemplary embodiment, nozzle  602  may receive the compound from compound storage  614  and mix the compound with fluid flowing through wall mounted sootblower  616 . Wall mounted sootblower  616  may carry the compound to any of a variety of utility furnaces. Wall mounted sootblower  616  may also deliver the compound to wall  630  or any targeted area of the furnace reachable by wall mounted sootblower  616 . 
     In various other embodiments, transport air valve  612  may also include components capable of attaching pressurized air to feed line  610 . For example, transport air valve  612  may also include a flow regulator, an air pressure regulator, and/or a filter. These components may enable transport air valve  612  to function as an air pressure source so that it is possible to add additional transport air to move larger heavier quantities of the compound. 
     In an exemplary embodiment of the present invention, and with reference to  FIG. 7 , retractable sootblower  716  may comprise feed tube  704  and valve  706 . In one exemplary embodiment nozzle  702  is inserted between feed tube  704  and valve  706 . For example nozzle  702  may be retrofitted into retractable sootblower  716 . In another example, retractable sootblower  716  may be originally constructed with nozzle  702  between feed tube  704  and valve  706 . In various exemplary embodiments, nozzle  702  may be a component of a compound feed mechanism  700  which comprises valve  708 , feed line  710 , transport air valve  712  and compound storage  714 . Valve  708  may be coupled to feed line  710 . Feed line  710  may be coupled to transport air valve  712 . Transport air valve  712  may be coupled to compound storage  714 . 
     In an exemplary embodiment nozzle,  702  may receive the compound from compound storage  714  and mix the compound with fluid flowing through retractable sootblower  716 . In various examples, the sootblower may be a Long Retract Diamond Power Model IK-525 or a Long Retract Clyde Bergemann Model US. Sootblower  716  may comprise any device configured to deliver fluid into the interior of any of a variety of utility furnaces. Specifically, lance  718  and injection nozzle  720  may extend into the interior of a utility furnace. Retractable sootblower  716  may then deliver the compound to, for example, the wall, superheat pipes, or any targeted area of the furnace reachable by retractable sootblower  716 . 
     In various exemplary embodiments of the present invention, the nozzle can be placed in line with any commercially available or custom built sootblower including but not limited to a wall sootblower, long retractable sootblower, rotating element sootblower, helical sootblower, and rake-type blower. The nozzle may be included as a constituent piece of the valve, the feed tube, or a combination of either. Furthermore, the sootblowers may be installed on a furnace before adding the nozzle and compound feed. Alternatively a sootblower can be installed on a furnace after it has been retrofitted with a nozzle. 
     In accordance with various exemplary embodiments, an apparatus mixes a compound with a pressurized fluid to be delivered into a utility furnace. The mixture of the compound and the pressurized fluid may occur inside the body of the nozzle or may occur as the nozzle delivers the compound and pressurized fluid to the feed tube. The nozzle functions to mix the compound with the pressurized fluid stream. This mixture of pressurized fluid and compound is then delivered into a furnace, either by means of a custom apparatus or commercial apparatus. Any apparatus that functionally delivers the fluid compound mixture to the furnace is contemplated herein. 
     For convenience a number of pressures and relative pressures may be discussed herein. For example, a first pressure may be the pressure at the poppet valve. This pressure is what is being put through the sootblower in the absence of the present invention. This pressure may also vary greatly due to a number of factors such as plant system pressure, poppet valve setting, and/or sootblower type. A second pressure may be the pressure at the chemical injection port. The second pressure is a function of the pressure drop across the nozzle. A third pressure discussed may be the pressure required to push the compound into the fluid stream running through the sootblower. The third pressure may be formed on or behind the compound in order to deliver it to the sootblower. The third pressure may be created by a pump. In instances where there is a sufficient vacuum at the chemical injection port or the second pressure, there may not need to be a third pressure to deliver compound. The pressures discussed herein are relative to atmospheric pressures. In various examples, functionality of the system with various commercially manufactured sootblowers was tested as shown in table 1. 
     
       
         
           
               
               
               
               
               
             
               
                 TABLE 1 
               
               
                   
               
               
                   
                   
                 Pressure 
                 Pressure at 
                 Displacement 
               
               
                 Sootblower 
                   
                 at Poppet 
                 Chemical 
                 Pump 
               
               
                 Manufacturer 
                 Medium 
                 Valve 
                 Injection Port 
                 Pressure 
               
               
                   
               
             
            
               
                 Copes Vulcan 
                 Steam 
                 390 PSI 
                     38 PSI 
                 60 PSI 
               
               
                 T-40 
               
               
                 Clyde Bergmann 
                 Steam 
                 230 PSI 
                      5 PSI 
                 20 PSI 
               
               
                 US Blower 
               
               
                 Diamond Power 
                 Air 
                 165 PSI 
                 −2.5 PSI 
                 10 PSI 
               
               
                 IK-525 Blower 
               
               
                   
               
            
           
         
       
     
     In various examples, such as the test performed on the Copes Vulcan T-40 (see Table 1), the pressure of the fluid at the poppet valve in a utility furnace may be maximized in an attempt to deal with extreme slagging. In some instances the fluid pressures at the poppet valves may be operated at higher pressures than the utility furnace manufacture recommended pressure settings. High poppet valve pressures may translate into high chemical injection port pressures. In such instances, a pump may be used to increase the compound pressure in order to overcome the pressure at the chemical injection port. Furthermore, depending on the situation and/or the type of mechanism used to overcome the chemical injection port pressures, the compound may be introduced as a wet slurry in order to ease introduction into the pressurized stream. 
     In other examples, such as the test performed on the Clyde Bergmann US Blower (see Table 1), lower fluid pressures at the poppet valve correspond to lower fluid pressures at the chemical injection port. In such instances, lower pressures from the pump may be used in order to overcome the pressure at the chemical injection port. Again, the compound may be introduced as a wet slurry in order to ease introduction into the pressurized stream. 
     In still other examples, such as the test performed on the Diamond Power IK-525 Blower (see Table 1), the still lower pressures at the poppet valve illustrate the vacuum that may be created at the nozzle allowing substantially easier introduction of the compound into the furnace regardless whether it is slurried or in dry form. 
     While the pressures at the poppet valve of the various sootblowers in the industry may vary greatly depending on the type and condition of the sootblowers or the conditions of the medium, utility furnace, or other factors, it should be noted that the systems, devices, and methods discussed herein are beneficial in adapting the sootblowers to receive and disperse various compounds in the utility furnace regardless of the countless variations. 
     In accordance with various aspects of the invention, as discussed above, the delivery mechanism may be any permanent or temporary fixture on the utility furnace. In various exemplary embodiments of the present invention, a delivery mechanism is any component capable of delivering the pressurized fluid and/or mix of compound and fluid into a utility furnace. 
     As may be typical of a burner in a utility furnace, the burner can be vertical or horizontal, having air blowers located around the burner. On the outlet of the air blower are devices with movable flaps or vanes that control the shape and pattern of the flame from the burner. These air blowers can be classified as primary secondary and tertiary depending on when the air is introduced into the furnace. Primary air is the first air introduced into the furnace. Primary air is the first combustion air added to fuel being carried into the burner. Secondary air is used to supplement and finely tune the primary air. Compound may be injected into the furnace by supplying compound via plant utility air to the burner front. Then by routing high temperature tubing (or similar material) from the burner front, outside the furnace, to the internal combustion air delivered by the air blower devices. 
     In accordance with various embodiments, as illustrated in  FIGS. 8   a  and  8   b , the compound may be delivered into the utility furnace through the burner. For example, the compound may be delivered to the primary air at or near the burner and introduced into the furnace with the primary air. Primary air provides the initial ignition oxygen for mixture with the fuel and subsequent combustion. In another example, the compound may be delivered to the secondary air at or near the burner and introduced into the furnace with the secondary air. Secondary air is additional carefully controlled air flow that allows the higher hydrocarbons to burn (e.g., trim air). In another example, the compound may be delivered with tertiary air. Tertiary air insures delayed combustion purposely for NOx combustion (e.g., super trim air used on low NOx burners). In various examples, the compound may be delivered to the furnace interior at the burners through any air transport or openings available. 
     In accordance with various embodiments, a mixing chamber  802  may be located in the fluid supply  820 . As may be typical of a utility furnace, the fluid supply  820 , which may be instrument air and/or plant utility air, may be routed to the burner front. The compound may be delivered from the compound delivery device  814  through delivery tube  810  and valve  812  to the mixing chamber  802 . In the mixing chamber the compound may be mixed with the plant utility air under pressure. The mixture of the compound and the pressurized fluid may then travel through the fluid supply  820  to the burner front  824 . Fluid supply line  820  may have a valve  822  to shut off compound delivery and/or regulate supply air to the burner. From the burner front  824 , high temperature line  840  may be routed to the air blowers  830  in the burner. As the high temperature line  840  between the burner front  824  and the air blowers  830  is likely not present on a commercial burner, the high temperature line  840  may need to be routed in the field on the burner. In one example, high temperature line  840  may deliver compound to the primary air. In one example, high temperature line  840  may deliver compound to the secondary air. In one example, high temperature line  840  may deliver compound to the tertiary air. In on example, high temperature line  840  may deliver compound to one or more of the primary, secondary, or tertiary air. The air from the air blowers carrying the compound exits the burner into the utility furnace. 
     The compound when introduced into the utility furnace adds a benefit over the already available pressurized fluid. In one exemplary embodiment, MgHO 2  is the compound. In this example, MgHO 2  may be delivered by sootblowers to slag coated steam/water pipes to aid in the removal of slag. In this example, the MgHO 2  is suited specifically to breaking up a variety of slag accumulations caused by coal based fuels burned inside of the utility furnace. 
     In another exemplary embodiment, magnesium is added into a utility furnace to aid in the encapsulation of harmful by products. In other exemplary embodiments, magnesium, kaolin, mullite, and/or other beneficial agents or combinations of these agents can be introduced into the utility furnace. These agents can be introduced into the utility furnace, superheats, back pass, preheats, exhaust stream, or other location to aid in the encapsulation of SO 2 . 
     In another exemplary embodiment, multiple compounds can be injected into the sootblowers to deal with inclement conditions such as low temperature. Dry has its advantages in extreme cold temperatures in the sootblower in the furnace; dry injection is a good option for injecting in the ducts and the discharge of the air pre-heaters. However due to difficulties in delivering dry compound at higher pressures, poly-ethylene glycol (PEG) mixed with other chemicals discussed above, for example, MgHO 2 , may be a good combination as an alternative to dry injection in extreme low temperature conditions. In accordance with one embodiment, the PEG can be effectively mixed with the compound at 55-60% solids by weight. Furthermore, the PEG is EPA compliant to inject in the furnace. In various other embodiments, the mixture of PEG and compound can be effective for dusting when transporting coal. Thus this combination functions as a dust inhibitor and slag suppressor. 
     In accordance with an exemplary embodiment and with reference to  FIG. 9 , a method is provided for introducing a solid compound into a furnace. The method comprises retrofitting a sootblower with a nozzle, such as nozzle  400   a  in  FIG. 4   a  (step  910 ). Attaching the nozzle to a compound feed and receiving a compound into the nozzle (step  920 ). Supplying a fluid through a sootblower (step  930 ). Mixing the compound with the fluid (step  940 ). Transporting the compound and fluid through a feed tube into a utility furnace (step  950 ). Various exemplary embodiments may further comprise, reacting the compound in the utility furnace (step  960 ). Furthermore, in one exemplary embodiment, the method includes removing the nozzle (which was installed in step  910 ) from the system (step  970 ). 
     In accordance with an exemplary embodiment, a user may retrofit the nozzle by installing it on an operational sootblower in use on any utility furnace (step  910 ). For example, the user may separate the poppet valve and feed tube in a sootblower (step  912 ) and insert a nozzle by removably connecting the nozzle between the valve and the feed tube (step  914 ). When separating the valve and the feed tube the fastening mechanism is removed. For example, in some commercially used sootblowers this mechanism is a 600 pound flange with four ½ in NPT studs. In accordance with various embodiments the user may need to replace the studs that originally held the feed tube and the poppet valve together. The new studs may need to be longer in order to make up the new distance added by the nozzle. For example when placing a nozzle inline with some commercial feed tubes and valves, 2 inch longer studs may be used. The user may reconnect the valve and the feed tube with the nozzle in between (step  916 ). 
     In accordance with and exemplary embodiment, the user may attach the nozzle to a compound feed mechanism (step  920 ). As discussed above the compound feed mechanism may deliver compound to the nozzle in a number of ways. In accordance with one embodiment of the present invention, the compound is drawn into the nozzle by a vacuum created at the nozzle. This vacuum may create a transport air stream. The compound may be inserted into the transport air stream in a variety of ways including but not limited to physical force (e.g., an auger), pressure, gravity, or vacuum. However, it may be possible to overload the transport air by introducing too much compound (i.e., extreme loading) or too heavy a compound. When extreme loading or moving very heavy solids occurs, additional transport may be needed. As such, in accordance with another embodiment, the transport air may be pressurized coming from the compound feed. For example, the pressurized feed can come from plant instrument air and connect at the transport air valve ( 612  of  FIG. 6  or  712  of  FIG. 7 ) of the compound feed mechanism. Likewise, in some embodiments the nozzle may only create a static or lower pressure condition. In which case the compound may be pumped to the nozzle in order to provide sufficient pressure to overcome the pressure at the nozzle. 
     In accordance with an exemplary embodiment, fluid may be supplied through a sootblower (step  930 ). In one example, the fluid supply may be initiated by opening the poppet valve. In accordance with various other exemplary embodiments, the fluid supply may be initiated according to the individual operation of the sootblower or other fluid supply and delivery device. 
     In accordance with one embodiment of the present invention, the compound may be mixed with the pressurized fluid (step  940 ). In one exemplary embodiment the compound may be combined with fluid supply into a laminar flow. The compound may be control fed into the transport flow stream. In one exemplary embodiment and with exemplary reference to  FIG. 7 , valve  708  may be opened after the sootblower is started. In one exemplary embodiment, transport air is pulled by a vacuum through the compound feed mechanism into the sootblower fluid stream. In another exemplary embodiment, the compound is forced through the nozzle by a pump. The pump may be a part of the compound feed mechanism. The compound may be delivered to nozzle  702  in response to the injection nozzle  720  being in the correct location in the interior of the utility furnace. The delivery of the compound may be triggered by activating the transportation device which may be, for example, an auger feeder, transport air, or a pump. As discussed before, the fluid stream pressures at the poppet valve can vary greatly. As such, the chemical injection port pressure (i.e., the fluid pressure after the nozzle) may also vary greatly. The variations may be adapted to by adjusting the pressure created by the pressure device in compound feed mechanism and compound storage mechanism (for example, the pump, auger, and/or transport air). The mixing or infusion may occur after fluid has been running through the sootblower. Due to the nozzle creating a vacuum, the peak impact pressure (i.e., the pressure designed into the sootblower system as measured at the injection nozzle  720  to allow it to effectively move ash in a furnace) may drop. In an exemplary embodiment, this pressure drop is compensated for by readjustment of the poppet valve. This compensation may thus prevent negative effects on the cooling flow of the lance tube and/or the peak impact pressure. Similar, measures may be taken for a mixing chamber. While the mixing chamber may not cause the same pressure drop as the nozzle any pressure drop due to the mixing chamber can be compensated for. 
     In accordance with one embodiment of the present invention, the mixture of pressurized fluid and compound may then be advantageously supplied to targeted portions of a utility furnace (step  950 ). Such locations may normally be accessible only by means of the sootblower. For example, referring to  FIGS. 2   a ,  2   c ,  2   d , and  2   e , various elements away from the wall may be the target. Referring to  FIG. 2   b , the wall may be the target. Furthermore sootblowers are located throughout substantially the entire utility furnace. As such, in various embodiments a user is able to deliver the mixture to a utility furnace through all types of manufactured sootblowers. The use of any sootblower in the utility furnace allows for covering areas accessible by the sootblowers. Furthermore, the delivery of the compound by the sootblowers installed on the utility furnace is possible without relying on flue gas. As such reliance on the changing flue gas flow dynamics is avoided. Ultimately the quantity of chemical delivered can also be minimized through the targeted effort. 
     In accordance with one embodiment of the present invention, the mixture may react with the targeted elements on the interior of the furnace (step  960 ). Introducing the compound into a utility furnace may improve the efficiency of the furnace. This is done by impregnating the compound to affected slagging areas and chemically altering the buildup of pollution, slag, or other deleterious elements in furnace. In an exemplary embodiment, the device is configured to more easily remove the slag after first chemically reacting with the slag. In one example, this may allow the furnace to function on less fuel while maintaining substantially similar operating parameters. 
     In accordance with one embodiment of the present invention, the nozzles may be removed from the sootblower when finished distributing the compound into the furnace (step  970 ). This will restore the sootblower to its original condition. Once removed the nozzle and compound feed mechanism may be stored for use on the same sootblower or they may be moved to another sootblower. In accordance with another embodiment of the present invention, the nozzle and/or compound feed mechanism may be left in place for future use. 
     It may be understood herein with regard to the various aspects, embodiments and examples of the present invention, that a compound, for providing environmental benefits to emissions gases, reducing slagging, and/or improving the overall efficiency of a utility furnace, may be injected into the utility furnace through preexisting fluid systems (e.g., compressed air systems) by mixing the compound with the fluid in the fluid systems. The mixture may be injected into the utility furnace through one more of preexisting devices on the furnace including burners, sootblowers, access panels, fuel delivery, etc. 
     As stated above, the compound may be any of a variety of solids, liquids, or gases that may beneficially be injected into a utility furnace. In accordance with an example embodiment, the compound may comprise a fuel. In an example embodiment, the compound comprises a fuel that is substantially different from the primary fuel used to fire the utility furnace. For example, if the primary fuel for firing a utility furnace is coal, the compound may comprise a fuel that is not coal. For example, the compound may comprise a combustible gas or a liquid fuel. In one example, a solid fuel is a different type of fuel from a liquid fuel or a gas fuel. In an example embodiment, the compound can comprise a fuel such as natural gas liquid (NGL), natural gas (NG), methane, propane, butane, gasoline, fuel oil, #6 Bunker C, petroleum, biofuels, liquefied coal, hydrocarbon fuels, and/or the like. In one example, if the primary fuel is coal, the compound may comprise NGL. In another example, if the primary fuel is fuel oil, the compound may comprise methane. In an example embodiment, liquefied natural gas (LNG) is pure methane in a liquid form, and NGL is primarily ethane and a combination of heavier hydrocarbons in a liquid form. The LNG or NGL may be in a liquid form under pressure, but may vaporize when injected into the combustion air. 
     Adding a compound, such as a second fuel, to the furnace via a retrofit to the burner front, can facilitate improvement of at least one of harmful emissions and slagging in a utility furnace. Various improvements are related to the reduced quantity of coal being burned. Nevertheless, despite the reduction in coal firing the utility furnace, performance can be maintained with the addition of the second fuel. Thus, retrofit of a coal plant by adding a second fuel type to the combustion, for example by adding NGL, facilitates a reduction in particulate matter. The retrofit can facilitate reduced slagging and fouling. The method of reducing the coal supplied to the furnace is configured to reduce the fly ash produced, and thus reduce the amount of slagging that may occur. The reduction of coal is also configured to reduce greenhouse gasses created in the utility furnace. For example, there can be a nearly linear reduction in NOx, SOx and ash compared to the coal reduction. Thus, in an example embodiment, the retrofit burners at the utility furnace can be operated to consume between 1%-35% less coal that at base load prior to the retrofit. This means that NOx, Sox, and ash can be reduced as much as 1%-35% as well. Similarly, as much as 35% less reagents can be used in the furnace. For example, if 35% less coal is used, 35% less ammonia could be used in the furnace. Clearly, a great environmental benefit can be achieved by reducing these greenhouse gasses, particulates, and reagent use. 
     Moreover, the ability to flexibly vary the amount or proportion of primary fuel and secondary fuel is highly beneficial. In one example embodiment, once the retrofit is complete, the proportion of primary to secondary fuel can be adjusted without making any structural changes to the burner front. This is in stark contrast to prior art retrofits that convert a single fuel fired utility furnace to a co-fired furnace. In the past, such retrofits would remove burners from the burner front and replace them with the second fuel burner. Not only are such retrofits very expensive and time consuming, they are somewhat permanent operations. For example, in a prior art retrofit, the burner front may be modified to remove coal inputs and replace them with a second fuel such as specifically designed fuel oil inputs. At that point, if for any reason one does not want to use or loses a supply of the second fuel, the retrofit utility furnace is only able to continue operating at reduced capacity (if at all) with the single fuel. A similarly expensive overhaul would be needed to return the utility furnace to its former operating capacity. 
     In contrast, in accordance with an example embodiment, a utility furnace can be retrofit inexpensively and with flexibility. The furnace retrofit is configured to facilitate flexible operation of the utility furnace in either single or dual fire mode, and/or to vary the ratio of the primary and secondary fuel. This flexibility can be achieved without a shutdown, overhaul, or physical rework of the burner front. In an example embodiment, the ratio or operating mode can be changed while the furnace is operating. In another embodiment, the changes are simply made when the furnace is not operating. Thus, in an example embodiment, the change in ratio or operating mode is made by selecting the desired fuel source supply rates. The retrofit can be done without replacing the burner front, and in such a manner that the original installation functional operation can be returned to without any renovations to the burner front. In other words, after adding the ability to add a second fuel to the combustion air provided at the burner front, the utility furnace can be flexibly operated 100% on coal, or in dual fuel mode without any structural changes. It is noted that even a dual fired burner could be retro-fit, according to the principles described herein, to add a third fuel source. 
     In an example embodiment, the reduction BTU&#39;s caused by reducing the primary fuel is offset by adding the second (new) fuel. In this example embodiment, the original BTU rating for the burner is not exceeded, but the burner can be operated at, near, or below its designed BTU rating. In this way, the retrofit of the burner front may be configured to not significantly change the operation of the furnace or require collateral changes to other systems. 
     As additional benefits, this flexibility facilitates the operators of the utility furnace to take advantage of changing commodity prices of various fuels on a constant basis and over long periods of time, without any costs to make structural changes, or delay to implement the new operation parameters. Similarly, this flexibility facilitates the operators of the utility furnace to make adjustments to achieve environmental compliance standards/metrics/goals. Again, this flexibility is very helpful in the event that a fuel source becomes temporarily unavailable. For example, if the secondary fuel is natural gas and the natural gas pipeline is shut down for some reason, the utility furnace can adjust to quickly return to single fired mode at 100% capacity until the natural gas pipeline is functional again. Again, the flexibility described herein may facilitate supply chain moderating, such as if a plant begins to have too much coal piled on site due to a long over haul, the plant can adjust the proportions of the two fuels to adjust the rate of use of one of the two fuels to balance out on site storage of that fuel, as desired. 
     In one example embodiment, the compound may be indirectly added to the fluid supply that is injected into the furnace. For example, and with reference to  FIG. 8 , the compound may be mixed with instrument air or clean/dry air that in turn conveys the compound to the combustion air (similar for sootblowers). This is most likely to occur when the compound is a solid. In another example embodiment, the compound is directly added to the fluid supply that is injected into the furnace. For example, the compound may be added directly to the combustion air (e.g., primary air, secondary air, and/or tertiary air). In this example embodiment, the space around the burner in the burner front can be the mixing chamber in which the combustion air and compound are mixed. For example, a gas, such as NGL can be directly delivered to the burner front, and added to the combustion air at or near the burner front. 
     It is noted, that throughout this disclosure various references have been made to use of plant instrument air, service air, soot blowing air, steam, or pressurized water sources. To the extent these fluid sources are pre-existing, which they often are, they are also generally installed with redundancy and reliability measures in place. Thus, in an example embodiment, the fluid stream used to inject the compound is a reliable, redundant, pre-existing fluid stream. This facilitates a relatively inexpensive but reliable function for the injected compound compared to use of separate and new sources of the fluid stream. 
     With reference now to  FIG. 10 , a burner front  1000  can comprise a primary burner tube  1010  having a primary outlet  1011 , a water-tube burner opening  1030 , various air dampers, and a second fuel pipe  1020 . In an example embodiment, a second fuel can be conveyed to burner front  1000  via second fuel pipe or supply pipe (the “source” of the second fuel)  1020 . The pipe  1020  may be configured to enter the burner front and to deliver the second fuel in the second fuel pipe  1020  to a point  1021  near the primary burner outlet. The outlet of the second fuel pipe may be located in contact with or close to the primary fuel burner. In the example of a coal plant, a primary fuel coal burner tube has an outlet opening near the burner opening into the furnace. The coal burner tube is configured to blow coal powder into a furnace  1050 . The second fuel pipe, for example, may be oriented to similarly blow the second fuel into the furnace through the same burner opening  1030  in the water walls. In an example embodiment, the outlet of the second fuel pipe  1020  is behind or even with the outlet  1011  of the first fuel pipe  1010  (relative to the water-tube burner opening  1030 ) so that the coal abrasives do not wear down the second fuel pipe. 
     In an example embodiment, the second fuel pipe outlet  1021  lies in the windbox or combustion air box  1060 . In an example embodiment, the outlet  1021  of the second fuel pipe is located between the outer diameter of the coal pipe and the inner walls of the windbox. The windbox delivers combustion air to the furnace. This combustion air comprises primary, secondary and tertiary air. This air both carries and surrounds the fuel injected into the furnace. In an example embodiment, the windbox is the mixing chamber. In one example embodiment, it is noted that the proximity of the mixing chamber (i.e., the windbox) to the furnace means that the compound (fuel) and the combustion air may be coming together just as they enter the furnace or just before entering the furnace. Nevertheless, the combustion air conveys the compound (second fuel) into the furnace along with the primary fuel (e.g., coal). 
     In an example embodiment, the second fuel is injected in the combustion air in the vicinity of the burner. Many different burner designs exist, so the routing of the compound injection line (the second fuel line) may vary depending on the burner type being retro-fit. Nevertheless, the principle may be the same for each burner design. For example, with NG, LNG, or NGL, the fuel line may be field routed based on the burner design. The fuel line, in an example embodiment, is routed through the combustion air path. See, e.g.,  FIG. 10 . For example, the fuel line may be routed on the outside of the burner tube (e.g., the coal burner tube), and in the combustion air flowing past the burner tube. In an example embodiment, the fuel line  1020  is a pipe ending in a nozzle ring near the outlet  1011  of burner tube  1010  outside the burner tube. In an example embodiment, the pipe and nozzle ring are insulated from the coal burner tube, and/or is configured to stand off from burner tube  1010 . This may facilitate a reduction in radiant heat to the fuel tube. Thus, in an example embodiment, the nozzles (header ring) is in the combustion air path, and not in the coal path. For example, the pipe may enter the air box, and run along or near the burner pipe, stopping short of or equal with the burner pipe tip. In an example embodiment, the secondary fuel pipe  1020  comprises high temperature tubing or a similar material pipe. In an example embodiment, the pipe and header for the secondary fuel source does not extend past the exit of the coal burner pipe so as to not be in the flow of the coal being blown into the furnace. 
     In accordance with an example embodiment, a method of retrofitting a utility furnace, specifically retrofitting an existing burner on the utility furnace is provided. In this example embodiment, prior to the retrofit of the existing burner, the burner is configured to supply a single, first (original) fuel to the utility furnace. The example method comprises retrofitting the existing burner to be capable of supplying a second fuel to the utility furnace, wherein the second fuel is not the same as the first (original) fuel used on that burner. After the retrofit of the existing burner, the retrofit burner can change operation between co-fired mode and single fired mode or vary the proportions of the two fuels without physical rework to the burner. In this example embodiment, the first fuel is a solid and the second fuel is a liquid or gas. In another example embodiment, the first fuel is a gas and the second fuel is a liquid. In another example embodiment, the first fuel is a liquid and the second fuel is a gas. In another example embodiment, the second fuel type is one of: a liquid and a gas. In another example embodiment, the second fuel type is NGL. In another example embodiment, the second fuel type is LNG. In another example embodiment, the first fuel is supplied to the furnace in a coal burner tube and the second fuel is supplied to the furnace through a second tube located outside of and proximate to the coal burner tube, wherein both the coal burner tube and the second tube are located in the burner front windbox. 
     In one example embodiment, second pipe  1020  may be field routed along or near the coal burner tube. Near the end of the burner tube, the second pipe may circle a portion of burner tube  1010  to form a header tube with nozzles for injecting the second fuel into the combustion air. In an example embodiment, any suitable nozzle can be used, and the nozzle size can be determined based on flow rate of the gas or liquid. In an example embodiment, the nozzles are oriented to spray the second fuel in a direction perpendicular to the fuel pipe. In this manner, the second fuel is mixed with the combustion air and carried into the furnace. Moreover, any suitable nozzle orientation can be used. 
     In an example embodiment, the second pipe may have one or more valves to isolate the second fuel from burner front  1000 . For example, the second fuel pipe may have Class IV shut off valves  1071 , modulating control valves  1072 , and or the like. In various example embodiments, the valves may be manual valves or automatically controlled valves, such as program logic control valves or distributed control system valves. The valves may be configured to work with the burner management system or the combustion management system. 
     It is noted that the second fuel pipe and delivery mechanism is very different from a typical fuel oil lighter. Lighters typically cannot be modulated—they are generally binary on/off devices. Lighters are also typically limited in size and BTU output because they are only used to get the furnace started or to facilitate a controlled stop. Lighters cannot generate, for example, 30% or more of the furnace BTU&#39;s. 
     In an example embodiment, the second fuel may be supplied via a pipe from a source of that particular fuel. For example, the second pipe may be an NGL supply line. In another example embodiment, the pipe may be supplied from an onsite storage tank. For example, a large compressed natural gas or LNG or NGL storage tank could provide the fuel source. The second fuel may be supplied, for example, under pressure. In various embodiments, if the fuel is a liquid, it can be atomized before entrainment in an air stream. Any suitable atomizing nozzle/technology can be used to atomize the liquid fuel. 
     As discussed above, the compound can comprise various substances, chemicals, fuels, and the like. In particular, the stoichiometry of the reaction when the compound is injected is very often temperature dependent. In other words, injecting the compound at the wrong temperature could result in a less than complete reaction or no reaction at all. An advantage of injecting the compound through the pre-existing sootblowers and/or burner front, is that there are a very large number of points within the furnace and backend flue gases for selecting where to make the injection. There is a significant diversity of temperatures across these various injection points. Thus, in an example embodiment, the pre-existing sootblower locations provide a selection of temperature diverse locations for injection of the compound. For example, H 2 O 2  may advantageously be injected through the duct blowers spanning the economizer. 
     In the following description and/or claims, the terms coupled and/or connected, along with their derivatives, may be used. In particular embodiments, connected may be used to indicate that two or more elements are in direct physical contact with each other. Coupled may mean that two or more elements are in direct physical contact. However, coupled may also mean that two or more elements may not be in direct contact with each other, but yet may still cooperate and/or interact with each other. Furthermore, couple may mean that two objects are in communication with each other, and/or communicate with each other, such as two pieces of hardware. Furthermore, the term “and/or” may mean “and”, it may mean “or”, it may mean “exclusive-or”, it may mean “one”, it may mean “some, but not all”, it may mean “neither”, and/or it may mean “both”, although the scope of claimed subject matter is not limited in this respect. 
     It should be appreciated that the particular implementations shown and described herein are illustrative of various embodiments including its best mode, and are not intended to limit the scope of the present disclosure in any way. Furthermore, the connecting lines shown in the various figures contained herein are intended to represent exemplary functional relationships and/or physical couplings between the various elements. It should be noted that many alternative or additional functional relationships or physical connections may be present in a practical system. 
     While the principles of the disclosure have been shown in embodiments, many modifications of structure, arrangements, proportions, the elements, materials and components, used in practice, which are particularly adapted for a specific environment and operating requirements, can be made without departing from the principles and scope of this disclosure. These and other changes or modifications are intended to be included within the scope of the present disclosure and may be expressed in the following claims. 
     Statements of Example Embodiments: 
     In an example first embodiment, an apparatus comprises: a mixing chamber configured to receive a compound operable to improve at least one of harmful emissions and slagging in a utility furnace, wherein the mixing chamber is further configured to mix the compound with a fluid to be injected into the utility furnace, and wherein the fluid is delivered by a fluid supply which is in place at the utility furnace. In this example embodiment, the mixing chamber receives the compound from a compound feed mechanism. In this example embodiment, the mixing chamber is configured to be retrofitted between a valve and a feed tube. In this example embodiment, the valve and the feed tube are located on a sootblower. In this example embodiment, the mixing chamber is an integrated component of a sootblower. 
     In an example second embodiment, a method comprises: attaching a compound feed to a mixing chamber connected inline with a fluid supply; supplying the compound to the mixing chamber; mixing the compound with a fluid; and delivering the compound and the fluid to a utility furnace. In this example embodiment, the compound is supplied from a hopper to the mixing chamber by at least one of a vacuum and a pump. In this example embodiment, the fluid is delivered to a sootblower. In this example embodiment, the method further comprises: retrofitting the sootblower with the mixing chamber, wherein retrofitting comprises: separating a feed tube and a valve on the sootblower; inserting the mixing chamber between the feed tube and the valve; and connecting the mixing chamber, the feed tube, and the valve together. In this example embodiment, the mixing chamber is located near a burner and the compound is delivered to the utility furnace via a burner front of the utility furnace. In this example embodiment, the fluid supply is one of: plant instrument air, service air, sootblowing air, steam, and pressurized water sources. In this example embodiment, the plant instrument air is connected into the secondary air of the burner on the utility furnace and the compound is delivered from the mixing chamber, via the plant instrument air, into the secondary air and out of the burner front into the utility furnace. In this example embodiment, the compound is Magnesium Hydroxide. In this example embodiment, the fluid is combustion air that comprises one of: primary air, secondary air, and tertiary air. In this example embodiment, the compound is a fuel. In this example embodiment, the fluid is combustion air that comprises one of: primary air, secondary air, and tertiary air, and wherein the compound is a fuel comprising natural gas liquid (NGL). In these example embodiments, the compound is a gas or a liquid. 
     In a third example embodiment, a system comprises: a fluid supply delivering a fluid under pressure for use at a utility furnace; a compound capable of improving efficiency of the utility furnace; a mixing chamber operable to combine the fluid under pressure with the compound wherein, the mixing chamber is configured to be removably connected to the fluid supply; and a mechanism connected to the fluid supply that directs the fluid under pressure into the utility furnace. In this example embodiment, the system further comprises: a hopper configured to hold a quantity of the compound, wherein the mixing chamber is configured to receive the compound from the hopper; and a pump system configured to deliver the compound from the hopper to the mixing chamber at a pressure sufficient to overcome the pressure of the fluid under pressure. In this example embodiment, the compound is Magnesium Hydroxide. In this example embodiment, the mechanism is a sootblower having a valve, a feed tube, and a delivery device connected to the fluid supply, wherein the mixing chamber is connected inline between the valve and the feed tube. In this example embodiment, the compound, hopper, pump system, and mixing chamber are integrated with at least one of a retractable or a wall mounted sootblower installed on the utility furnace. In this example embodiment, the mechanism is a burner front in the utility and the fluid supply is a plant instrument air routed into a secondary air in the burner front, wherein the mixing chamber is on the plant instrument air, wherein the compound is delivered from the hopper to the mixing chamber and mixed with the fluid under pressure in the plant instrument air and then routed to the secondary air in the burner front and out of the burner front and into the utility furnace. In this example embodiment, the system is adjustable to operate the fluid supply at the same peak impact pressure with the mixing chamber as compared to without the mixing chamber. In this example embodiment, the compound is added directly to the fluid in the mixing chamber. In this example embodiment, the compound is atomized at about the same time it is injected into the fluid. 
     In a fourth example embodiment, a method of retrofitting a utility furnace, wherein the utility furnace has a burner front, wherein the burner front fires the utility furnace with a first fuel type, and wherein the burner front supplies combustion air associated with the combustion of the first fuel type, wherein the combustion air comprises at least one of: primary air, secondary air, and tertiary air, the method comprises: connecting a source of a second fuel type to the burner front, wherein the connection is configured to introduce the second fuel type into the combustion air; wherein the first fuel type is a different type of fuel from the second fuel type. In this example embodiment, the utility furnace is a coal fired furnace and the first fuel type is coal. In this example embodiment, the second fuel type is one of: a liquid and a gas. In this example embodiment, the second fuel type is natural gas liquid (NGL). In this example embodiment, the second fuel type is liquefied natural gas (LNG). In this example embodiment, the second fuel type is introduced directly into the combustion air. In this example embodiment, the second fuel type is introduced indirectly into the combustion air. 
     In a fifth example embodiment, a method of injecting a compound into a utility furnace comprises: injecting a compound into a preexisting fluid stream; wherein the preexisting fluid stream is a fluid stream carried in an already existing conveyance device, wherein the already existing conveyance device was connected to the utility furnace, in such a manner as to inject the preexisting fluid stream into the utility furnace, prior to retrofitting the utility furnace to provide the ability to inject the compound into the fluid stream; injecting the preexisting fluid stream, containing the compound, into the utility furnace through one of a burner front and a sootblower; and wherein the compound comprises one of: a solid, a liquid, and a gas. In this example embodiment, the preexisting fluid stream is one of primary, secondary, and tertiary air. In this example embodiment, the compound is one of: a liquid and a gas. In this example embodiment, the compound is a fuel other than a primary fuel for firing the utility furnace. In this example embodiment, the preexisting fluid stream and the compound are injected into the utility furnace through the burner front. In this example embodiment, the primary fuel is coal and wherein the compound comprises natural gas liquid (NGL). 
     In a sixth example embodiment, a method of injecting a compound into a utility furnace comprises: delivering a compound into the utility furnace by injecting the compound into a delivery mechanism conveying a combustion air, wherein the combustion air is one of primary air, secondary air, and tertiary air, wherein the compound comprises a fuel that is not a primary fuel for firing the utility furnace. In this example embodiment, the delivery mechanism is a burner front for the utility furnace, wherein the burner front comprises the burner and wherein the burner front is configured to mix the compound with the combustion air. In this example embodiment, the fuel is natural gas liquid (NGL) and the primary fuel is coal. 
     In a seventh example embodiment, a utility furnace comprises: a burner; a delivery mechanism, wherein the delivery mechanism is configured to deliver combustion air into the utility furnace, wherein the delivery mechanism is configured to deliver combustion air into the utility furnace in the vicinity of the burner, wherein the combustion air comprises one of primary air, secondary air and tertiary air; a fuel source provided to the burner, wherein the fuel source is a first fuel type and is the primary source of fuel to the utility furnace; and a compound source, connected to the delivery mechanism, wherein the compound source is configured to supply the compound into the combustion air in the delivery mechanism. In this example embodiment, the compound is a second fuel type different from the first fuel type. In this example embodiment, the second fuel type is one of: a liquid and a gas. In this example embodiment, the second fuel type is natural gas liquid (NGL). In this example embodiment, the second fuel type is liquefied natural gas (LNG). In this example embodiment, the first fuel is supplied to the utility furnace in a coal burner tube and wherein the second fuel is supplied to the utility furnace through a second tube located outside of and proximate to the coal burner tube, wherein both the coal burner tube and the second tube are located in a windbox of the burner front. 
     In an example embodiment, any of the preceding example embodiments may be combined with others of the presented example embodiments set forth above.