Patent Application
20120000200
The subject matter disclosed herein relates to waste heat recovery systems employing boilers, and more specifically, to inert gas purging systems for heat recovery boilers.
Waste heat recovery systems may be employed to recover low-grade heat, such as heat with a temperature below approximately 500° C., from industrial and commercial processes and operations. For example, waste heat recovery systems may be employed to recover low-grade heat from hot exhaust gases produced by gas turbines. Waste heat recovery systems that implement an Organic Rankine Cycle (ORC) by circulating an organic working fluid may be particularly efficient at recovering low-grade heat due to the relatively low phase change enthalpies of organic working fluids.
In a first embodiment, a system includes a valve system switchable between a waste heat recovery position configured to direct incoming exhaust gas through an interior volume of an exhaust section of an engine and a bypass position configured to direct the incoming exhaust gas through a bypass duct to bypass a heat recovery boiler disposed within the interior volume. The system also includes an inert gas purging system configured to inject an inert gas into the interior volume to displace residual exhaust gas from the interior volume.
In a second embodiment, a system includes a heat recovery boiler configured to absorb heat directly from exhaust gas within an exhaust section of an engine to heat an organic working fluid within the heat recovery boiler, an expander configured to expand the heated organic working fluid, a condenser configured to condense the expanded organic working fluid, a pump configured to direct the condensed organic working fluid to the heat recovery boiler, a sensor configured to detect a leak of the organic working fluid from the heat recovery boiler, and an inert gas purging system configured to inject inert gas into the exhaust section in response to detection of the leak.
In a third embodiment, a method includes detecting a leak of an organic working fluid from a heat recovery boiler into an interior volume of an exhaust section of an engine, setting a valve to a bypass position to direct incoming exhaust gas to bypass the interior volume of the exhaust section in response to detecting the leak, and injecting an inert gas into the interior volume to displace residual exhaust gas from the interior volume in response to detecting the leak.
These and other features, aspects, and advantages of the present invention will become better understood when the following detailed description is read with reference to the accompanying drawings in which like characters represent like parts throughout the drawings, wherein:
One or more specific embodiments of the present invention will be described below. In an effort to provide a concise description of these embodiments, all features of an actual implementation may not be described in the specification. It should be appreciated that in the development of any such actual implementation, as in any engineering or design project, numerous implementation-specific decisions must be made to achieve the developers' specific goals, such as compliance with system-related and business-related constraints, which may vary from one implementation to another. Moreover, it should be appreciated that such a development effort might be complex and time consuming, but would nevertheless be a routine undertaking of design, fabrication, and manufacture for those of ordinary skill having the benefit of this disclosure.
When introducing elements of various embodiments of the present invention, the articles “a,” “an,” “the,” and “said” are intended to mean that there are one or more of the elements. The terms “comprising,” “including,” and “having” are intended to be inclusive and mean that there may be additional elements other than the listed elements.
The present disclosure is directed to waste heat recovery systems that employ inert gas purging systems for heat recovery boilers. The waste heat recovery systems may recover low-grade heat from a system, such as a gas turbine, by implementing an Organic Rankine Cycle (ORC) with an organic working fluid, such as a hydrocarbon fluid or refrigerant. Rather than transferring heat to the organic working fluid through an intermediate fluid, such as oil, the present systems may employ a “direct” heat recovery boiler that transfers heat directly from the gas turbine exhaust gas to the working fluid. According to certain embodiments, the heat recovery boiler, which circulates the working fluid, may be disposed directly in the path of the exhaust gas within the exhaust section of the gas turbine. Placing the heat recovery boiler directly in the path of the exhaust gas, rather than using a secondary loop to transfer heat between the exhaust gas and the waste heat recovery system, may increase the overall efficiency of the waste heat recovery system, as well as reducing capital and/or operational costs.
To protect the gas turbine exhaust section and the waste heat recovery system in the event of a leak in the heat recovery boiler, the power generation system may employ a purging system for the heat recovery boiler. According to certain embodiments, the purging system may be enabled upon detection of a leak in the heat recovery boiler. The purging system may redirect the flow of exhaust gases so that the exhaust gases bypass the heat recovery boiler. Further, the purging system may inject an inert gas into the exhaust gas duct to purge residual exhaust gases from the exhaust duct. The inert gas also may cool the heat recovery boiler and dilute any leaking fluid, thereby extinguishing and/or inhibiting flames within the exhaust duct.
As shown in
The gas turbine engine 12 includes an air intake section 20, a compressor 22, a combustor section 24, a turbine 26, and an exhaust section 28. The turbine 26 is coupled to the compressor 22 via a shaft 30. Air 32 may enter the gas turbine engine 12 through the intake section 20 and flow into the compressor 22 where the air may be compressed to provide compressed air 34 to the combustor section 24. Within the combustor section 24, the compressed air 34 may mix with fuel in a fuel-to-air ratio that facilitates combustion of the fuel to produce combustion gases 36. According to certain embodiments, the combustor section 24 may include multiple combustors disposed annularly around the shaft 30.
From the combustor section 24, the hot combustion gases 36 may flow through the turbine 26 to drive the compressor 22 and/or the first load 14 via the shaft 30. For example, the combustion gases 36 may apply motive forces to turbine rotor blades within the turbine 26 to rotate the shaft 30. After flowing through the turbine 26, the hot combustion gases may exit the gas turbine engine 12 as exhaust gases 38 that flow through the exhaust section 28 to exit the gas turbine engine 12.
As the exhaust gases 38 flow through the exhaust section 28, the exhaust gases 38 may flow through an heat recovery boiler 40 that may absorb heat from the exhaust gases 38 to produce cooled exhaust gases 42. The heat recovery boiler 40 is located directly in the flow path of the exhaust gases 38 so that the exhaust gases 38 may transfer heat directly to a working fluid flowing through the heat recovery boiler 40. The cooled exhaust gases 42 may then exit the exhaust section 28 and may be directed through ductwork 43 to a stack 44 where the gases may be vented to the atmosphere.
As described further with respect to
As the exhaust gases 38 flow through the heat recovery boiler 40 disposed within the exhaust gas path of the exhaust section 28, the hot exhaust gases 38 may transfer heat to a working fluid flowing through the heat recovery boiler 40 within a working fluid loop 50. According to certain embodiments, the heat recovery boiler 40 may be a fin and tube heat exchanger that allows the working fluid to be circulated within the working fluid loop 50 directly in the path of the exhaust gases 38. Accordingly, the exhaust gases 38 may transfer heat directly to the working fluid circulating within the waste heat recovery system 16, rather than transferring heat through an intermediate loop, such as an oil loop.
According to certain embodiments, the waste heat recovery system 16 may circulate an organic working fluid within the working fluid loop 50 to recover waste heat from the exhaust gases 38. Any suitable organic working fluid, such as a hydrocarbon fluid or refrigerant, may be employed. The use of an organic working fluid may be particularly well suited to the waste heat recovery loop 50 due to the relatively low phase change enthalpy of the organic working fluid. According to certain embodiments, the organic working fluid may be an organic, high molecular mass, fluid that has a higher vapor pressure and lower critical temperature than water.
As the working fluid flows through the heat recovery boiler 40, the working fluid may absorb heat from the exhaust gases 38 causing all, or a substantial portion of the working fluid to change from a liquid phase to a vapor phase. The heated working fluid may then flow to an expander generator set 52 where the working fluid may be expanded to drive the second load 18. For example, the expander generator set 52 may include an expander that may be coupled to a generator to produce electricity from the expansion of the heated working fluid. From the expander generator set 52, the working fluid may flow to a condenser 54 where the working fluid may be condensed. According to certain embodiments, the condenser 54 may be an air-cooled heat exchanger. However, in other embodiments, any suitable type of condenser may be employed.
The condensed working fluid may then flow through a pump 58 that returns the working fluid to the heat recovery boiler 40 where the process may begin again. In other embodiments, additional equipment, such as valves, temperature and/or pressure sensors or transducers, receivers, and the like, may be included in the waste heat recovery system 16. For example, in certain embodiments, a recuperator or preheater may be included upstream from the heat recovery boiler 40 to preheat the working fluid before it enters the heat recovery boiler 40. Further, the waste heat recovery system 16 may be installed as part of a new power generation system 10 and/or may be retrofit into an existing power generation system 10. For example, in certain embodiments, an existing gas turbine 12 may be retrofitted with a waste heat recovery system 16 that disposes a heat recovery boiler 40 in the exhaust gas section 28.
As shown in
As shown in
After the exhaust gases 38 flow through the heat recovery boiler 40, the cooled exhaust gases 42 may exit the exhaust section 28 and enter the stack 44 through an inlet 63. As discussed above, because the working fluid circulating within the finned tubes 62 may be potentially flammable, it may be desirable to remove the exhaust gases 38 from the interior volume 60 in the event of a leak in the finned tubes 62. Accordingly, in the event of a leak, rather than directing the exhaust gases 38 through the opening 58 to the interior volume 60, the exhaust gases 38 may be directed through an opening 64 to flow through the bypass duct 46, as shown generally by arrows 65 in
To redirect the flow of the exhaust gases 38 through the bypass duct 46, a system of one or more valves 66 may be employed, which are switchable between a waste heat recovery position as shown in
In the waste heat recovery position, the valve 66 may be positioned to direct the exhaust gases 38 through the interior volume 60, as shown in
In the waste heat recovery mode shown in
When the bypass mode is enabled as shown in
The bypass duct 46 may be employed when a leak is detected in the finned tubes 62 of the heat recovery boiler 40. Accordingly, one or more sensors 68 may be employed to detect a leak in the finned tubes 62. For example, in embodiments where the working fluid is a hydrocarbon fluid, the sensor 68 may measure the level of hydrocarbons in the exhaust gas exiting the interior volume 60. An increased level of hydrocarbons may indicate a leak within the finned tubes 62. In another example, the sensor 68 may be designed to detect presence of a flame in or around the heat recovery boiler 40, such as by measuring ultraviolet light. The presence of a flame may indicate a leak within the finned tubes 62. In yet another example, multiple sensors 68, such as multiple hydrocarbon sensors, multiple flame detection sensors, or combinations thereof, may be employed. Further, in other embodiments, the sensor 68 may be designed to measure other parameters indicative of the composition of the exhaust gases 38. According to certain embodiments, the sensor 68 may be located in the inlet 63 to the stack 44. However, in other embodiments, the sensor 68 may be positioned within the interior volume 60.
The sensor 68 may be communicatively coupled to a controller 70 that may be used to change the position of the valve 66. For example, the controller 70 may receive an input, such as a hydrocarbon level, from the sensor 68 that indicates that a leak is present in the finned tubes 62. In response to receiving the input, the controller 70 may send a control signal to the valve 66 to move the valve to close opening 58, as shown in
The controller 70 also may govern operation of an inert gas injection system 72 that may be used to purge residual exhaust gases 38 from the interior volume 60 after the valve 66 has been moved to the bypass position. The inert gas injection system 72 may include an inert gas supply 74, such as one or more high pressure gas cylinders, which supplies inert gases for the inert gas injection system 72. As used herein, the term “inert gases” shall mean any gas or mixture of gases suitable to suppress combustion, prevent explosion, or extinguish a flame, primarily by dilution and/or displacement of oxygen in the exhaust gas. According to certain embodiments, the inert gases may include nitrogen and/or carbon dioxide.
Piping 76 may be used to direct the inert gases from the inert gas supply 74 into the interior volume 60. A valve 78 may be included within the piping 76 to regulate the flow of the inert gases from the tank 74 into the interior volume 60. For example, the valve 78 may be closed when the system is operating in a waste heat recovery mode to prevent the inert gases from entering the interior volume 60 and may be opened to allow the inert gases to enter the interior volume 60 when the system is operating in the bypass mode. Further, in certain embodiments, the valve 78 may be employed to increase and decrease the flow rate of the inert gases into the interior volume 60. Although only one valve 78 is shown in
The controller 70 may govern the operation of the inert gas injection system 72 through the valve 78. According to certain embodiments, the controller 70 may open the valve 78 in response to detecting a leak to allow the inert gases to enter the interior volume 60. The inert gases may enter the interior volume through one or more nozzles 79 that may inject the inert gases into the interior volume 60 from the piping 76. According to certain embodiments, the nozzles 79 may allow the inert gases to be injected into the interior volume 60 at relatively high flow rates. Further, the nozzles 79 may be located along the top, bottom, and/or sides, as well as around the exhaust gas inlet area, of the interior volume 60.
As the inert gases enter the interior volume 60, the inert gases may displace residual exhaust gases 38 within the interior volume 60 causing the residual exhaust gases to exit the interior volume 60 and enter the stack 44 through the inlet 63. Accordingly, when bypass mode is enabled, the flap 69 may remain open for a certain period of time to allow the residual exhaust gases to exit the interior volume 60 through the inlet 63. After the residual exhaust gases have exited the interior volume 60, the flap 69 may be closed, as shown in
After valve 78 has been opened to allow the inert gases to enter the interior volume 60, the controller 70 may stop operation of the pump 58 that circulates the working fluid through the heat recovery boiler 40. When the pump 58 is stopped, the working fluid may evaporate from the heat recovery boiler 40 and collect within the working fluid loop 50. Accordingly, additional working fluid may be inhibited from leaking into the interior volume 60 through the heat recovery boiler 40.
In response to detecting a leak, the controller 70 may set (block 86) the valve to the bypass position. For example, as shown in
After setting the valve 66 to the bypass position, the controller 70 then may inject (block 88) purge gas into the interior volume 60. For example, the controller 70 may activate the inert gas purging system by opening valve 78 to allow the inert gases to flow into the interior volume 60 through the nozzles 79. The inert gases may then purge residual exhaust gases 38 from the interior volume 60 by displacing the residual exhaust gases 38 from the interior volume 60 to the stack 44 through the inlet 63. As noted above with respect to
After the interior volume 60 has been purged of the exhaust gases 38, repairs may be conducted to repair any leaks within the heat recovery boiler 40. For example, the finned tubes 62 may be repaired or replaced. After the repairs have been completed, the valve 66 may be reset to the waste heat recovery position, as shown in
This written description uses examples to disclose the invention, including the best mode, and also to enable any person skilled in the art to practice the invention, including making and using any devices or systems and performing any incorporated methods. The patentable scope of the invention is defined by the claims, and may include other examples that occur to those skilled in the art. Such other examples are intended to be within the scope of the claims if they have structural elements that do not differ from the literal language of the claims, or if they include equivalent structural elements with insubstantial differences from the literal language of the claims.
