US20150000249A1 - Combined cycle power plant - Google Patents
Combined cycle power plant Download PDFInfo
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- US20150000249A1 US20150000249A1 US14/488,788 US201414488788A US2015000249A1 US 20150000249 A1 US20150000249 A1 US 20150000249A1 US 201414488788 A US201414488788 A US 201414488788A US 2015000249 A1 US2015000249 A1 US 2015000249A1
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- 230000008929 regeneration Effects 0.000 claims abstract description 38
- 238000011069 regeneration method Methods 0.000 claims abstract description 38
- 239000002912 waste gas Substances 0.000 claims abstract description 38
- 238000000746 purification Methods 0.000 claims abstract description 24
- 239000007789 gas Substances 0.000 claims abstract description 21
- 238000011084 recovery Methods 0.000 claims abstract description 20
- 239000006096 absorbing agent Substances 0.000 claims abstract 8
- 239000012530 fluid Substances 0.000 claims abstract 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 14
- 239000001569 carbon dioxide Substances 0.000 claims description 14
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000000446 fuel Substances 0.000 claims description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical class [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 5
- 229910002090 carbon oxide Inorganic materials 0.000 abstract description 4
- 230000001172 regenerating effect Effects 0.000 abstract description 4
- -1 amine carbonate Chemical class 0.000 description 20
- 150000001412 amines Chemical class 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 230000001105 regulatory effect Effects 0.000 description 3
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
- F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
- F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
- F01K23/10—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C6/00—Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas-turbine plants for special use
- F02C6/18—Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas-turbine plants for special use using the waste heat of gas-turbine plants outside the plants themselves, e.g. gas-turbine power heat plants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1456—Removing acid components
- B01D53/1475—Removing carbon dioxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/62—Carbon oxides
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K13/00—General layout or general methods of operation of complete plants
- F01K13/006—Auxiliaries or details not otherwise provided for
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
- F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
- F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
- F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
- F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
- F01K23/08—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with working fluid of one cycle heating the fluid in another cycle
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2252/00—Absorbents, i.e. solvents and liquid materials for gas absorption
- B01D2252/20—Organic absorbents
- B01D2252/204—Amines
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/504—Carbon dioxide
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
- Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/32—Direct CO2 mitigation
Definitions
- the present invention relates to a combined cycle power plant (CCPP) comprising a gas turbine plant, a heat recovery steam generator (HRSG) heated with hot exhaust gases from the gas turbine plant, and a steam turbine plant driven by the generated steam.
- CCPP combined cycle power plant
- HRSG heat recovery steam generator
- Such a CCPP is shown in U.S. Pat. No. 5,839,269.
- a steam turbine plant is provided with a high pressure turbine, a medium pressure turbine and a low pressure turbine, whereby high pressure and medium pressure steam is produced in the steam generator for driving the high pressure or medium pressure turbine, and the steam expanded in the medium pressure turbine is used to drive the low pressure turbine.
- steam with reduced low pressure can be channeled off from a sufficiently hot feed water tank of the steam generator and fed into a medium stage of the low pressure turbine through appropriate steam inlets.
- U.S. Pat. No. 5,839,269 discloses a range of measures for optimizing the design of gas turbine plants and for optimizing the operation of gas turbines.
- Gas turbine plants and other large combustion plants are typically operated with fuels based on hydrocarbons. This inevitably generates carbon oxides during operation, especially carbon dioxide, which is a green house gas and harmful to the environment, and should therefore be separated from the waste gases of the gas turbine plant.
- known waste gas purification plants can be used which are arranged downstream of the respective combustion process and which have an absorbing section and a regenerating section. Carbon dioxide which is carried along within the absorbing section, through which the particular waste gases are flowing, can be absorbed at relatively low temperature using an amine-H 2 O-system with the formation of a relatively concentrated amine carbonate solution.
- the concentrated amine carbonate solution can be subsequently converted in a regeneration section at high temperature into a relatively weak concentration amine-carbonate-solution, whereby carbon dioxide is released and led away and subsequently collected and stored.
- amine systems for example systems using chilled ammonia, can also be used.
- the purpose of the invention is thereby to connect a CCPP with a waste gas purification plant in an optimized way to supply the necessary thermal energy for heating the regeneration section of the purification plant and to use the residual heat for increasing the performance of the steam turbine plant.
- a waste gas purification plant is provided downstream of the gas turbine plant and the heat recovery steam generation plant, the gas purification plant comprising an absorbing section and a regenerating section, whereby inside the absorbing section, through which the waste gases flow, carbon dioxide which is carried in the waste gases is absorbed by an amine-H 2 O-system at relatively low temperature forming (relatively) high concentrations of amine carbonate solution, and whereby the concentrated amine carbonate solution is converted into a relatively weak amine carbonate solution in the regeneration section at an elevated temperature giving off carbon dioxide which is led away, whereby the regeneration section can be heated with steam, and the relatively weak amine carbonate solution generated in the regeneration section having an elevated temperature can be supplied via a heat exchanger back into the absorbing section for reuse, and thermal energy can be exchanged in the heat exchanger between the relatively weak concentration of amine carbonate solution and the relatively high concentration of amine carbonate solution being supplied to the regeneration section.
- the heat for the regeneration of the amine solution is introduced into the regeneration section by way of steam from the steam turbine and/or the steam generator, and the heat from the regenerated amine solution, having an elevated temperature, is used for preheating the high concentration amine carbonate solution led away from the absorbing section.
- the thermal energy required for regeneration of the amine solution can thereby be substantially reduced.
- the regeneration section is heated with saturated steam at a specified temperature. It is advantageous that the temperature level is only dependent on the steam pressure, so that the desired temperature can be regulated with the steam pressure.
- the steam for heating the regeneration section can be taken from the connection between the outlet of the medium pressure turbine and the inlet of the low pressure turbine.
- the hot condensate generated from heating the regeneration section can be supplied to an evaporator of the heat recovery steam generator in order to produce additional steam with low pressure, the steam can then be supplied to a stage of the low pressure turbine, whereby this steam can, if necessary, be channeled through a superheater of the steam generator before being introduced into the low pressure turbine, in order to increase its power output.
- the thermal energy which may need to be conducted away from the absorbing section, can be used to preheat the feed water for the steam generator.
- the steam circuits therefore only need to be slightly modified, according to the invention, to supply the necessary thermal energy for the waste gas purification plant and/or to use resulting residual heat for increasing the performance of the steam turbine plant, i.e. the hot condensate is used in a new, additional pressure level (compared to the standard water-steam cycle.
- the regeneration of the amine solution in the regeneration section can be carried out at a temperature of 126° C. as opposed to a possible process temperature of about 145° C., whereby the separation of the carbon dioxide out of the high concentration amine carbonate solution supplied to the regeneration section happens at a less than optimal process temperature.
- This is accepted here because the necessary thermal energy for heating the regeneration section is thereby disproportionally reduced, so that the performance of the CCPP and its efficiency can be substantially increased.
- only a relatively small loss of performance must be tolerated compared to a CCPP without downstream waste gas purification.
- the hot condensate or pressurized water is supplied to at least one flash evaporator and allowed at least partly to evaporate there at low pressure so that additional steam is released for operating the steam turbine plant, in particular for the low pressure steam turbine of the steam turbine plant.
- Usable steam for operating the low pressure turbine of the steam turbine plant is produced with little effort by introducing hot condensate or pressurized water into the at least one flash boiler, where it boils due to a fast reduction in pressure and evaporates.
- the physical effect is thereby exploited whereby the boiling point of a liquid is dependent on pressure, and accordingly a hot liquid starts to boil suddenly when it is introduced into a space having low pressure and therefore at least partially evaporates.
- a series of flash boilers can be provided, whereby pressurized water or condensate from a first flash boiler is supplied to a second flash boiler which has a lower inner pressure compared to the first flash boiler, so that the pressurized water or condensate, coming out of the first flash boiler, can at least partially evaporate here.
- further flash boilers can be arranged in a cascade. The flash boilers in the flash boiler cascade thereby produce steam with accordingly different pressure levels, whereby the steam of each flash boiler is supplied to an appropriate stage of the turbine, in particular to the low pressure turbine of the steam turbine plant.
- the steam coming from a flash boiler can, if necessary, be superheated with the heat recovery steam generator plant of the CCPP in order to drive the respective turbine section more effectively.
- FIG. 1 a highly schematized representation of a CCPP according to the invention
- FIG. 2 a schematized representation of a waste gas purification plant according to the invention
- FIG. 3 a representation of an advantageous connection of the regeneration section of the waste gas purification plant to a CCPP or its steam generator or its low pressure steam turbine of the steam turbine plant
- FIG. 4 a schematized representations for the use of a hot condensate or pressurized water from the power plant or waste gas purification plant
- FIG. 5 an advantageous variation of the arrangement shown in FIG. 3 .
- the CCPP comprises a gas turbine plant 1 , which can have a generally known construction, for example as in the above mentioned U.S. Pat. No. 5,839,269, and having a compressor 11 , at least one combustion chamber 12 and a gas turbine 13 .
- the hot waste gases 100 of the gas turbine plant 1 then flow through a heat recovery steam generator 2 .
- a waste gas purification plant 4 Arranged downstream of the heat recovery steam generator 2 is a waste gas purification plant 4 , which is described below.
- the steam produced in the heat recovery steam generator 2 drives a steam turbine plant 5 .
- the gas turbine plant 1 and the steam turbine plant 5 can drive generators 3 or the like respectively, whereby it is possible in principle to couple the rotor shafts R of the gas turbine plant 1 with those of the steam turbine plant 5 and use a common generator 3 .
- a steam circuit For driving the steam turbine plant 5 a steam circuit can be provided as described in the following:
- Water is fed by a pump 7 from a feed water tank 6 into a heater 8 , which is arranged inside of a heat recovery steam generator 2 in the waste gas path.
- a heater 8 At the outlet of the heater 8 there is high pressure water with, for example, a pressure of 160 bar and a temperature of 300° C.
- a tube register 9 downstream of the heater 8 the high pressure water is evaporated and superheated, so that high pressure steam is available at the outlet of the tube register 9 .
- This superheated, high pressure steam is supplied to a high pressure steam turbine 51 of the steam turbine plant 5 , whereby the high pressure steam expands inside the high pressure turbine 51 .
- the steam expanded in this way, CRH (Cold Reheat), is subsequently supplied through a further tube register 10 , so that this steam is reheated.
- the steam from the tube register 10 is supplied to a medium pressure turbine 52 of the steam turbine plant 5 , whereby the steam expands in the medium pressure turbine 52 so that there is low pressure steam downstream of it, which, if necessary, can be further heated in a tube register (not shown) and supplied to a low pressure turbine 53 of the steam turbine plant 5 .
- the steam expanded in the low pressure turbine 53 subsequently flows into an air- or water-cooled condenser 109 .
- the condensate produced there is then supplied by a pump 111 back to the feed water tank 6 .
- the waste gas purification plant 4 comprises an absorbing section 41 through which the waste gas flows, and a regeneration section 42 in order to regenerate the absorbing medium from section 41 and to supply it back to the absorbing section 41 .
- a regeneration section 42 in order to regenerate the absorbing medium from section 41 and to supply it back to the absorbing section 41 .
- waste gases 1000 free of carbon oxides.
- the waste gases 100 flow through a bath of water and amine solution, whereby the carbon dioxide in the waste gases 100 is bonded by the water to form carbonic acid, which with the amines then forms a relatively high concentration of amine carbonate solution.
- This relatively high concentration of amine carbonate solution is supplied to the regeneration section 42 by a pump 113 .
- a high temperature is maintained, for example a temperature from about 120° to 145° C., at which the relatively high concentration of amine carbonate solution is converted into a relatively weak concentration of amine carbonate solution, giving off carbon dioxide in the process, whereby the carbon dioxide is supplied by a compressor 114 to a store or the like (not shown).
- the temperature necessary for the regeneration process in the regeneration section 42 can be maintained by circulating the relatively weak concentration of amine carbonate solution, produced in the regeneration section 42 , in a circuit through a heater 115 , which is itself heated with steam as described below.
- the relatively weak concentration of amine carbonate solution is supplied back to the absorbing section 41 by a pump 116 , whereby on returning the solution flows through a heat exchanger 112 through which the relatively high concentration of amine carbonate solution being supplied to the regeneration section 42 also flows (in opposite directions), so that the high concentration of amine carbonate solution supplied to the regeneration section 42 is pre-heated and the heater 115 requires a relatively low thermal input for maintaining the necessary temperature for the regeneration process.
- the heater 115 of the regeneration section 42 is preferably heated with steam, in particular saturated steam, which can be diverted off at point A in FIG. 1 in the steam path between the medium pressure steam turbine 52 and the low pressure steam turbine 53 of the steam turbine plant 5 .
- This channeled off steam condenses at or in the heater 115 whilst giving up heat to the relatively low concentration amine carbonate solution.
- the thereby generated condensate K the temperature of which is around the operating temperature of the regeneration section 42 , i.e. at a temperature between about 120° C. and 145° C., can then be supplied according to FIG. 3 to an evaporator 118 and therein heated with heat from the heat recovery steam generator 2 .
- the steam generated there, the pressure of which is below the pressure of the steam supplied to the inlet of the low pressure steam turbine can be subsequently superheated and supplied via appropriate steam inlets to an intermediate stage of the low pressure steam turbine 53 .
- the steam produced by the evaporator 118 can be supplied to the heater 115 together with the steam channeled off from point A, preferably superheated.
- the dotted line in FIG. 3 shows such option.
- the condensate K from the heater 115 can also be introduced into the feed water tank 6 so that, on the one hand, the feed water is accordingly heated.
- the condensate K from the heater 115 is used for producing steam having a very low pressure for introducing into an intermediate stage of the low pressure steam turbine 53 .
- the waste gas purification plant is therefore used to generate a fourth steam pressure level, in addition to the steam pressure levels for the high, middle, and low pressure steam turbines of the steam turbine plant 5 .
- the steam turbine plant 5 and the heat recovery steam generator 2 are only slightly modified by the waste gas purification plant 4 .
- the absorbing section 41 of the waste gas purification plant, through which the hot waste gases 100 flow, must be cooled in order to maintain the necessary low temperature for the absorption process.
- This temperature is about 40° C. in case of the amine system, and about 5° C. in case of the chilled ammonia process.
- the hot condensate K from heater 115 is supplied by a pump 116 to the inlet of a flash boiler 117 , whereby a regulating valve 118 is arranged at the inlet of the flash boiler 117 in order to maintain a pressure in the line between the flash boiler 117 and the pump 116 , whereby the pressure is above the boiling pressure of water at the prevailing temperature of the condensate K.
- the flash boiler 117 there is a lower pressure compared to the pressure in the line between the pump 116 and the flash boiler 117 , so that the condensate K introduced into the flash boiler 117 , to a greater or less extent, immediately evaporates (flashes to steam).
- the very low pressure steam produced the pressure of which is below the steam pressure at A in the steam path between the medium pressure turbine and the low pressure turbine, can now be supplied to an intermediate stage of the low pressure turbine 53 .
- the pressure and the quantity of the flashed steam, produced in the boiler 117 can be increased.
- the very low pressure steam from the flash boiler 117 can be superheated in a heater 119 before it is introduced into the low pressure turbine 53 .
- the heater 119 can itself be heated with steam from the outlet of the high pressure turbine (CRH) or preferably by flue gas in the heat recovery steam generator (HRSG). In principle any other heat source could also be used.
- FIG. 5 in place of a single flash boiler 117 , there can be a cascade of flash boilers 117 , 117 ′, 117 ′′, whereby the condensate coming from each flash boiler 117 , 117 ′ is supplied to a subsequent flash boiler 117 ′, 117 ′′ through a further regulating valve 118 ′, 118 ′′, whereby the pressure in the subsequent flash boiler 117 ′, 117 ′′ is lower than the pressure in the preceding flash boiler 117 , 117 ′, so that the condensate supplied to it partially evaporates quickly.
- the cascade may comprise three flash boilers 117 , 117 ′, 117 ′′, as shown in FIG. 5 .
- the pump 116 in FIGS. 4 and 5 can be used for increasing the hot condensate (K) pressure, so as to increase the pressure and quantity of the flashed steam.
- the steam flows, supplied to the low pressure steam turbine, can also be superheated in appropriate heaters 119 , before they are introduced into the low pressure steam turbine 53 .
- the heater 119 may be heated by steam from any suitable source.
- This embodiment is based on the general idea that condensed water exiting at relatively high temperature can be (partially) evaporated in flash boilers at low pressure, and the steam produced can be used for driving the steam turbine.
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Abstract
The invention relates to a combined cycle power plant that includes, a gas turbine plant, a heat recovery steam generator heated by hot waste gases of a gas turbine plant, and a steam turbine plant driven by the steam produced, and a waste gas purification plant, arranged downstream of the heat recovery steam generator in which carbon oxides in the waste gases can be absorbed by an absorber fluid, which is subsequently regenerated at an elevated temperature in a regenerating section while giving up the carbon oxides for supplying to a storage. The regenerating section has a heater for maintaining a necessary elevated temperature for regeneration. The heater operates with steam from the heat recovery steam generator or from the steam turbine plant. The steam condenses and the resulting hot condensate can be supplied to a flash boiler where it, at low pressure, immediately at least partially evaporates. This steam can be supplied to an appropriate stage of the steam turbine plant according to the steam pressure.
Description
- This application claims priority to PCT/EP2013/055881 filed Mar. 21, 2013, which claims priority to European application 12160585.1 filed Mar. 21, 2012 and European application 12185806.2 filed Sep. 25, 2012, all of which are hereby incorporated in their entireties.
- The present invention relates to a combined cycle power plant (CCPP) comprising a gas turbine plant, a heat recovery steam generator (HRSG) heated with hot exhaust gases from the gas turbine plant, and a steam turbine plant driven by the generated steam.
- Such a CCPP is shown in U.S. Pat. No. 5,839,269. In this known CCPP a steam turbine plant is provided with a high pressure turbine, a medium pressure turbine and a low pressure turbine, whereby high pressure and medium pressure steam is produced in the steam generator for driving the high pressure or medium pressure turbine, and the steam expanded in the medium pressure turbine is used to drive the low pressure turbine. In the CCPP of U.S. Pat. No. 5,839,269 it is also provided that steam with reduced low pressure can be channeled off from a sufficiently hot feed water tank of the steam generator and fed into a medium stage of the low pressure turbine through appropriate steam inlets.
- In addition U.S. Pat. No. 5,839,269 discloses a range of measures for optimizing the design of gas turbine plants and for optimizing the operation of gas turbines.
- Gas turbine plants and other large combustion plants are typically operated with fuels based on hydrocarbons. This inevitably generates carbon oxides during operation, especially carbon dioxide, which is a green house gas and harmful to the environment, and should therefore be separated from the waste gases of the gas turbine plant. In principle, known waste gas purification plants can be used which are arranged downstream of the respective combustion process and which have an absorbing section and a regenerating section. Carbon dioxide which is carried along within the absorbing section, through which the particular waste gases are flowing, can be absorbed at relatively low temperature using an amine-H2O-system with the formation of a relatively concentrated amine carbonate solution. The concentrated amine carbonate solution can be subsequently converted in a regeneration section at high temperature into a relatively weak concentration amine-carbonate-solution, whereby carbon dioxide is released and led away and subsequently collected and stored. In lieu of such amine systems other waste gas purification systems, for example systems using chilled ammonia, can also be used.
- From US 2011/0314815 A1 it is generally known to equip a CCPP as described above with a downstream waste gas purification plant. in US 2011/0314815 A1 it is shown that a waste gas purification plant with relatively small capacity can be sufficient, if the gas turbine plant is operated with exhaust gas recirculation in such a way that during combustion substantially only completely oxidized hydrocarbons, that is, carbon dioxide and water (and N2) remain. Otherwise, there is no indication towards an optimal integration of the waste gas purification plant into a CCPP.
- The purpose of the invention is thereby to connect a CCPP with a waste gas purification plant in an optimized way to supply the necessary thermal energy for heating the regeneration section of the purification plant and to use the residual heat for increasing the performance of the steam turbine plant.
- In particular, according to the invention, a waste gas purification plant is provided downstream of the gas turbine plant and the heat recovery steam generation plant, the gas purification plant comprising an absorbing section and a regenerating section, whereby inside the absorbing section, through which the waste gases flow, carbon dioxide which is carried in the waste gases is absorbed by an amine-H2O-system at relatively low temperature forming (relatively) high concentrations of amine carbonate solution, and whereby the concentrated amine carbonate solution is converted into a relatively weak amine carbonate solution in the regeneration section at an elevated temperature giving off carbon dioxide which is led away, whereby the regeneration section can be heated with steam, and the relatively weak amine carbonate solution generated in the regeneration section having an elevated temperature can be supplied via a heat exchanger back into the absorbing section for reuse, and thermal energy can be exchanged in the heat exchanger between the relatively weak concentration of amine carbonate solution and the relatively high concentration of amine carbonate solution being supplied to the regeneration section.
- According to a first aspect of the invention the heat for the regeneration of the amine solution is introduced into the regeneration section by way of steam from the steam turbine and/or the steam generator, and the heat from the regenerated amine solution, having an elevated temperature, is used for preheating the high concentration amine carbonate solution led away from the absorbing section. The thermal energy required for regeneration of the amine solution can thereby be substantially reduced.
- According to a preferred embodiment, the regeneration section is heated with saturated steam at a specified temperature. It is advantageous that the temperature level is only dependent on the steam pressure, so that the desired temperature can be regulated with the steam pressure.
- In the case of a steam turbine plant with a high pressure steam turbine, a medium pressure steam turbine and a low pressure steam turbine, the steam for heating the regeneration section can be taken from the connection between the outlet of the medium pressure turbine and the inlet of the low pressure turbine.
- According to an advantageous embodiment of the invention, the hot condensate generated from heating the regeneration section can be supplied to an evaporator of the heat recovery steam generator in order to produce additional steam with low pressure, the steam can then be supplied to a stage of the low pressure turbine, whereby this steam can, if necessary, be channeled through a superheater of the steam generator before being introduced into the low pressure turbine, in order to increase its power output.
- Advantageously, the thermal energy, which may need to be conducted away from the absorbing section, can be used to preheat the feed water for the steam generator.
- The steam circuits therefore only need to be slightly modified, according to the invention, to supply the necessary thermal energy for the waste gas purification plant and/or to use resulting residual heat for increasing the performance of the steam turbine plant, i.e. the hot condensate is used in a new, additional pressure level (compared to the standard water-steam cycle.
- According to a particularly advantageous embodiment of the invention the regeneration of the amine solution in the regeneration section can be carried out at a temperature of 126° C. as opposed to a possible process temperature of about 145° C., whereby the separation of the carbon dioxide out of the high concentration amine carbonate solution supplied to the regeneration section happens at a less than optimal process temperature. This is accepted here because the necessary thermal energy for heating the regeneration section is thereby disproportionally reduced, so that the performance of the CCPP and its efficiency can be substantially increased. As a result, only a relatively small loss of performance must be tolerated compared to a CCPP without downstream waste gas purification.
- According to another aspect of the invention the hot condensate or pressurized water is supplied to at least one flash evaporator and allowed at least partly to evaporate there at low pressure so that additional steam is released for operating the steam turbine plant, in particular for the low pressure steam turbine of the steam turbine plant.
- Usable steam for operating the low pressure turbine of the steam turbine plant is produced with little effort by introducing hot condensate or pressurized water into the at least one flash boiler, where it boils due to a fast reduction in pressure and evaporates. The physical effect is thereby exploited whereby the boiling point of a liquid is dependent on pressure, and accordingly a hot liquid starts to boil suddenly when it is introduced into a space having low pressure and therefore at least partially evaporates.
- According to a preferred embodiment of the invention, where appropriate, a series of flash boilers can be provided, whereby pressurized water or condensate from a first flash boiler is supplied to a second flash boiler which has a lower inner pressure compared to the first flash boiler, so that the pressurized water or condensate, coming out of the first flash boiler, can at least partially evaporate here. If necessary, further flash boilers can be arranged in a cascade. The flash boilers in the flash boiler cascade thereby produce steam with accordingly different pressure levels, whereby the steam of each flash boiler is supplied to an appropriate stage of the turbine, in particular to the low pressure turbine of the steam turbine plant.
- The steam coming from a flash boiler can, if necessary, be superheated with the heat recovery steam generator plant of the CCPP in order to drive the respective turbine section more effectively.
- Preferred features of the invention can be found in the claims and in the following description of the drawings by way of which particularly preferred embodiments of the invention are described in more detail.
- Protection is not only claimed for the indicated or shown combination of features but also for any combination of the shown or indicated individual features.
- The drawings show in:
-
FIG. 1 a highly schematized representation of a CCPP according to the invention, -
FIG. 2 a schematized representation of a waste gas purification plant according to the invention, -
FIG. 3 a representation of an advantageous connection of the regeneration section of the waste gas purification plant to a CCPP or its steam generator or its low pressure steam turbine of the steam turbine plant -
FIG. 4 a schematized representations for the use of a hot condensate or pressurized water from the power plant or waste gas purification plant, and -
FIG. 5 an advantageous variation of the arrangement shown inFIG. 3 . - According to
FIG. 1 the CCPP according to the invention comprises agas turbine plant 1, which can have a generally known construction, for example as in the above mentioned U.S. Pat. No. 5,839,269, and having acompressor 11, at least onecombustion chamber 12 and agas turbine 13. Thehot waste gases 100 of thegas turbine plant 1 then flow through a heatrecovery steam generator 2. Arranged downstream of the heatrecovery steam generator 2 is a wastegas purification plant 4, which is described below. The steam produced in the heatrecovery steam generator 2 drives asteam turbine plant 5. Thegas turbine plant 1 and thesteam turbine plant 5 can drivegenerators 3 or the like respectively, whereby it is possible in principle to couple the rotor shafts R of thegas turbine plant 1 with those of thesteam turbine plant 5 and use acommon generator 3. - For driving the steam turbine plant 5 a steam circuit can be provided as described in the following:
- Water is fed by a
pump 7 from afeed water tank 6 into aheater 8, which is arranged inside of a heatrecovery steam generator 2 in the waste gas path. At the outlet of theheater 8 there is high pressure water with, for example, a pressure of 160 bar and a temperature of 300° C. In atube register 9 downstream of theheater 8 the high pressure water is evaporated and superheated, so that high pressure steam is available at the outlet of thetube register 9. This superheated, high pressure steam is supplied to a highpressure steam turbine 51 of thesteam turbine plant 5, whereby the high pressure steam expands inside thehigh pressure turbine 51. The steam expanded in this way, CRH (Cold Reheat), is subsequently supplied through afurther tube register 10, so that this steam is reheated. The steam from thetube register 10 is supplied to amedium pressure turbine 52 of thesteam turbine plant 5, whereby the steam expands in themedium pressure turbine 52 so that there is low pressure steam downstream of it, which, if necessary, can be further heated in a tube register (not shown) and supplied to alow pressure turbine 53 of thesteam turbine plant 5. The steam expanded in thelow pressure turbine 53 subsequently flows into an air- or water-cooledcondenser 109. The condensate produced there is then supplied by apump 111 back to thefeed water tank 6. - According to
FIG. 2 , the wastegas purification plant 4 comprises an absorbingsection 41 through which the waste gas flows, and aregeneration section 42 in order to regenerate the absorbing medium fromsection 41 and to supply it back to the absorbingsection 41. At the outlet of the absorbingsection 41 there arewaste gases 1000 free of carbon oxides. - Inside the absorbing
section 41 thewaste gases 100 flow through a bath of water and amine solution, whereby the carbon dioxide in thewaste gases 100 is bonded by the water to form carbonic acid, which with the amines then forms a relatively high concentration of amine carbonate solution. This relatively high concentration of amine carbonate solution is supplied to theregeneration section 42 by apump 113. Inside the regeneration section 42 a high temperature is maintained, for example a temperature from about 120° to 145° C., at which the relatively high concentration of amine carbonate solution is converted into a relatively weak concentration of amine carbonate solution, giving off carbon dioxide in the process, whereby the carbon dioxide is supplied by acompressor 114 to a store or the like (not shown). - The temperature necessary for the regeneration process in the
regeneration section 42 can be maintained by circulating the relatively weak concentration of amine carbonate solution, produced in theregeneration section 42, in a circuit through aheater 115, which is itself heated with steam as described below. - The relatively weak concentration of amine carbonate solution is supplied back to the absorbing
section 41 by apump 116, whereby on returning the solution flows through aheat exchanger 112 through which the relatively high concentration of amine carbonate solution being supplied to theregeneration section 42 also flows (in opposite directions), so that the high concentration of amine carbonate solution supplied to theregeneration section 42 is pre-heated and theheater 115 requires a relatively low thermal input for maintaining the necessary temperature for the regeneration process. - The
heater 115 of theregeneration section 42 is preferably heated with steam, in particular saturated steam, which can be diverted off at point A inFIG. 1 in the steam path between the mediumpressure steam turbine 52 and the lowpressure steam turbine 53 of thesteam turbine plant 5. This channeled off steam condenses at or in theheater 115 whilst giving up heat to the relatively low concentration amine carbonate solution. The thereby generated condensate K, the temperature of which is around the operating temperature of theregeneration section 42, i.e. at a temperature between about 120° C. and 145° C., can then be supplied according toFIG. 3 to anevaporator 118 and therein heated with heat from the heatrecovery steam generator 2. The steam generated there, the pressure of which is below the pressure of the steam supplied to the inlet of the low pressure steam turbine, can be subsequently superheated and supplied via appropriate steam inlets to an intermediate stage of the lowpressure steam turbine 53. - Alternatively, the steam produced by the
evaporator 118 can be supplied to theheater 115 together with the steam channeled off from point A, preferably superheated. The dotted line inFIG. 3 shows such option. - Alternatively, the condensate K from the
heater 115 can also be introduced into thefeed water tank 6 so that, on the one hand, the feed water is accordingly heated. - As a result the condensate K from the
heater 115 is used for producing steam having a very low pressure for introducing into an intermediate stage of the lowpressure steam turbine 53. The waste gas purification plant is therefore used to generate a fourth steam pressure level, in addition to the steam pressure levels for the high, middle, and low pressure steam turbines of thesteam turbine plant 5. Thesteam turbine plant 5 and the heatrecovery steam generator 2 are only slightly modified by the wastegas purification plant 4. - It has proved advantageously to operate the
regeneration section 42 of the wastegas purification plant 4 at a relatively low temperature, which is actually suboptimal for the regeneration process. The thermal energy requirement of theheater 115 is thereby disproportionally reduced, with the result that the loss of performance of the CCPP, due to the necessary removal of thermal energy during the operation of the wastegas purification plant 4, is kept low. - The absorbing
section 41 of the waste gas purification plant, through which thehot waste gases 100 flow, must be cooled in order to maintain the necessary low temperature for the absorption process. This temperature is about 40° C. in case of the amine system, and about 5° C. in case of the chilled ammonia process. - According to an embodiment, shown in
FIG. 4 , the hot condensate K fromheater 115 is supplied by apump 116 to the inlet of aflash boiler 117, whereby a regulatingvalve 118 is arranged at the inlet of theflash boiler 117 in order to maintain a pressure in the line between theflash boiler 117 and thepump 116, whereby the pressure is above the boiling pressure of water at the prevailing temperature of the condensate K. In theflash boiler 117 there is a lower pressure compared to the pressure in the line between thepump 116 and theflash boiler 117, so that the condensate K introduced into theflash boiler 117, to a greater or less extent, immediately evaporates (flashes to steam). The very low pressure steam produced, the pressure of which is below the steam pressure at A in the steam path between the medium pressure turbine and the low pressure turbine, can now be supplied to an intermediate stage of thelow pressure turbine 53. By increasing the pressure of the hot condensateK using pump 116, the pressure and the quantity of the flashed steam, produced in theboiler 117, can be increased. - According to a preferred variation of this embodiment the very low pressure steam from the
flash boiler 117 can be superheated in aheater 119 before it is introduced into thelow pressure turbine 53. Theheater 119 can itself be heated with steam from the outlet of the high pressure turbine (CRH) or preferably by flue gas in the heat recovery steam generator (HRSG). In principle any other heat source could also be used. - According to another embodiment of the invention, as shown in
FIG. 5 , in place of asingle flash boiler 117, there can be a cascade offlash boilers flash boiler subsequent flash boiler 117′, 117″ through a further regulatingvalve 118′, 118″, whereby the pressure in thesubsequent flash boiler 117′, 117″ is lower than the pressure in the precedingflash boiler flash boilers FIG. 5 . - As mentioned above, the
pump 116 inFIGS. 4 and 5 can be used for increasing the hot condensate (K) pressure, so as to increase the pressure and quantity of the flashed steam. - In this way, steam flows having subsequently decreasing pressures can be directed from the flash boilers of the
flash boiler cascade pressure steam turbine 53. - In this embodiment the steam flows, supplied to the low pressure steam turbine, can also be superheated in
appropriate heaters 119, before they are introduced into the lowpressure steam turbine 53. Theheater 119 may be heated by steam from any suitable source. - This embodiment is based on the general idea that condensed water exiting at relatively high temperature can be (partially) evaporated in flash boilers at low pressure, and the steam produced can be used for driving the steam turbine.
Claims (10)
1. A combined cycle power plant (CCPP) comprising,
a gas turbine plant,
a heat recovery steam generator through which hot waste gases from the gas turbine plant flow,
a steam turbine plant driven by steam from the heat recovery steam generator, and
a waste gas purification plant, arranged downstream of the heat recovery steam generator, having an absorbing section in which carbon dioxide in the waste gases is absorbed by an absorber fluid, whereby the waste gas purification plant comprises a regeneration section which is supplied with the absorber fluid loaded with carbon dioxide, whereby the absorber fluid can be regenerated at an elevated temperature while giving up the carbon dioxide for supplying to a storage, and whereby the regenerated absorber fluid is supplied back into the absorbing section for absorbing the carbon dioxide in the waste gases, whereby the regeneration section comprises a heater which is heatable with the steam from the heat recovery steam generator or from the steam turbine plant, whereby the supplied steam condenses in or at the heater and the resulting hot condensate is supplied to at least one evaporator, where it is at least partially evaporated to steam and whereby this steam is introduced into a stage of the steam turbine plant, in particular into an intermediate stage of the low pressure turbine of the steam turbine plant.
2. The combined cycle power plant according to claim 1 , further comprising a heat exchanger is arranged between the absorber section and the regeneration section, whereby the absorber fluid from the regeneration section being led back into the absorbing section, and the absorber fluid from the absorbing section being supplied to the regeneration section through the heat exchanger.
3. The combined cycle power plant according to claim 1 , wherein the thermal energy extracted from the absorbing section is used for preheating fuel for the gas turbine plant or for preheating feed water for the steam turbine plant.
4. The combined cycle power plant according to claim 1 , wherein a part of the steam generated by the at least one evaporator is added to the steam supplied to the heater of the regeneration section.
5. The combined cycle power plant according to claim 1 , wherein the steam generated by the at least one evaporator is superheated in a heater of the heat recovery steam generator and then supplied to a middle stage of the low pressure turbine of the steam turbine plant.
6. The combined cycle power plant according to claim 1 , wherein the steam turbine plant comprises a high pressure steam turbine, a medium pressure steam turbine and a low pressure steam turbine, whereby steam is taken from a point between the outlet of the medium pressure steam turbine and the inlet of the low pressure steam turbine for heating the heater of the regeneration section.
7. The combined cycle power plant according to claim 1 , wherein the condensate is supplied to a cascade of flash boilers, whereby pressurized water or condensate from a first flash boiler is supplied to a second flash boiler which has a lower inner pressure relative to the first flash boiler, so that the pressurized water or condensate from the first flash boiler can at least partially evaporate, whereby the steam produced by the flash boilers is supplied to one or more stages of the steam turbine plant, in particular to the low pressure steam turbine, corresponding to their different pressures.
8. The combined cycle power plant according to claim 7 , wherein the steam from the at least one flash boiler is superheated, e.g. with the heat recovery steam generator, before being introduced into a stage of the steam turbine plant.
9. The combined cycle power plant according to claim 7 , wherein the steam from the at least one flash boiler is superheated by the steam, coming from the outlet of the high pressure steam turbine of the steam turbine plant.
10. The combined cycle power plant according to claim 1 , wherein the remaining condensate from the at least one evaporator is supplied to the feed water tank of the steam turbine plant.
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
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EP12160585 | 2012-03-21 | ||
EP12160585.1 | 2012-03-21 | ||
EP12185806.2 | 2012-09-25 | ||
EP12185806 | 2012-09-25 | ||
PCT/EP2013/055881 WO2013139884A2 (en) | 2012-03-21 | 2013-03-21 | Combined cycle power plant |
Related Parent Applications (1)
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PCT/EP2013/055881 Continuation WO2013139884A2 (en) | 2012-03-21 | 2013-03-21 | Combined cycle power plant |
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US20150000249A1 true US20150000249A1 (en) | 2015-01-01 |
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US14/488,788 Abandoned US20150000249A1 (en) | 2012-03-21 | 2014-09-17 | Combined cycle power plant |
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US (1) | US20150000249A1 (en) |
EP (1) | EP2828492A2 (en) |
CN (1) | CN104254673A (en) |
IN (1) | IN2014DN07990A (en) |
WO (1) | WO2013139884A2 (en) |
Cited By (4)
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WO2019084208A1 (en) * | 2017-10-25 | 2019-05-02 | Scuderi Group, Inc. | Bottoming cycle power system |
US10876432B2 (en) * | 2015-08-19 | 2020-12-29 | Kabushiki Kaisha Toshiba | Combined cycle power system with an auxiliary steam header supplied by a flasher and a surplus steam leak |
US11346544B2 (en) * | 2019-09-04 | 2022-05-31 | General Electric Company | System and method for top platform assembly of heat recovery steam generator (HRSG) |
US20230264953A1 (en) * | 2021-09-22 | 2023-08-24 | Saudi Arabian Oil Company | Integration of power generation with methane reform |
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CN105477977A (en) * | 2015-12-25 | 2016-04-13 | 武汉旭日华科技发展有限公司 | Energy saving method used for active carbon granule adsorbing and recovering device |
EP3219940B1 (en) | 2016-03-18 | 2023-01-11 | General Electric Technology GmbH | Combined cycle power plant and method for operating such a combined cycle power plant |
DE102016216437A1 (en) * | 2016-08-31 | 2018-03-01 | Dürr Systems Ag | Steam system and method for operating a steam system |
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CN1006996B (en) * | 1985-07-19 | 1990-02-28 | 克拉夫特沃克联合公司 | Combination gas and steam-turbine power station |
US5660037A (en) * | 1995-06-27 | 1997-08-26 | Siemens Power Corporation | Method for conversion of a reheat steam turbine power plant to a non-reheat combined cycle power plant |
DE19536839A1 (en) | 1995-10-02 | 1997-04-30 | Abb Management Ag | Process for operating a power plant |
US6256976B1 (en) * | 1997-06-27 | 2001-07-10 | Hitachi, Ltd. | Exhaust gas recirculation type combined plant |
DE10001995A1 (en) * | 2000-01-19 | 2001-07-26 | Alstom Power Schweiz Ag Baden | Method for setting or regulating the steam temperature of the live steam and / or reheater steamer in a composite power plant and composite power plant for carrying out the method |
CN1685187A (en) * | 2002-09-30 | 2005-10-19 | Bp北美公司 | Reduced carbon dioxide emission system and method for providing power for refrigerant compression and electrical power for a light hydrocarbon gas liquefaction process |
NO328975B1 (en) * | 2008-02-28 | 2010-07-05 | Sargas As | Gas power plant with CO2 purification |
EP2246532A1 (en) | 2008-12-24 | 2010-11-03 | Alstom Technology Ltd | Power plant with CO2 capture |
CN102300619B (en) * | 2009-01-28 | 2015-05-27 | 西门子公司 | Method And Device For Separating Carbon Dioxide From An Exhaust Gas Of A Fossil Fired Power Plant |
WO2011155886A1 (en) * | 2010-06-11 | 2011-12-15 | Klas Jonshagen | A system for supplying energy to a co2 separation unit at a power plant |
WO2012013596A1 (en) * | 2010-07-28 | 2012-02-02 | Sargas As | Jet engine with carbon capture |
-
2013
- 2013-03-21 CN CN201380015368.9A patent/CN104254673A/en active Pending
- 2013-03-21 EP EP13711044.1A patent/EP2828492A2/en not_active Withdrawn
- 2013-03-21 IN IN7990DEN2014 patent/IN2014DN07990A/en unknown
- 2013-03-21 WO PCT/EP2013/055881 patent/WO2013139884A2/en active Application Filing
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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US10876432B2 (en) * | 2015-08-19 | 2020-12-29 | Kabushiki Kaisha Toshiba | Combined cycle power system with an auxiliary steam header supplied by a flasher and a surplus steam leak |
WO2019084208A1 (en) * | 2017-10-25 | 2019-05-02 | Scuderi Group, Inc. | Bottoming cycle power system |
US11346544B2 (en) * | 2019-09-04 | 2022-05-31 | General Electric Company | System and method for top platform assembly of heat recovery steam generator (HRSG) |
US20230264953A1 (en) * | 2021-09-22 | 2023-08-24 | Saudi Arabian Oil Company | Integration of power generation with methane reform |
US12024430B2 (en) * | 2021-09-22 | 2024-07-02 | Saudi Arabian Oil Company | Integration of power generation with methane reform |
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CN104254673A (en) | 2014-12-31 |
EP2828492A2 (en) | 2015-01-28 |
WO2013139884A2 (en) | 2013-09-26 |
IN2014DN07990A (en) | 2015-05-01 |
WO2013139884A3 (en) | 2014-08-28 |
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