WO2006131283A2 - Dampferzeugungsanlage und verfahren zum betreiben und nachrüsten einer dampferzeuganlage - Google Patents
Dampferzeugungsanlage und verfahren zum betreiben und nachrüsten einer dampferzeuganlage Download PDFInfo
- Publication number
- WO2006131283A2 WO2006131283A2 PCT/EP2006/005334 EP2006005334W WO2006131283A2 WO 2006131283 A2 WO2006131283 A2 WO 2006131283A2 EP 2006005334 W EP2006005334 W EP 2006005334W WO 2006131283 A2 WO2006131283 A2 WO 2006131283A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- air
- steam
- line
- compressor
- flue gas
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 35
- 238000009420 retrofitting Methods 0.000 title claims description 9
- 239000003546 flue gas Substances 0.000 claims abstract description 55
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 48
- 238000002485 combustion reaction Methods 0.000 claims abstract description 45
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000001301 oxygen Substances 0.000 claims abstract description 25
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 16
- 238000000926 separation method Methods 0.000 claims description 29
- 238000010304 firing Methods 0.000 claims description 10
- 239000007789 gas Substances 0.000 claims description 8
- 239000003507 refrigerant Substances 0.000 claims description 4
- 238000009835 boiling Methods 0.000 claims description 3
- 238000007689 inspection Methods 0.000 claims description 3
- 230000010354 integration Effects 0.000 claims 2
- 238000001816 cooling Methods 0.000 claims 1
- 238000009434 installation Methods 0.000 claims 1
- 238000005194 fractionation Methods 0.000 abstract 2
- 241000196324 Embryophyta Species 0.000 description 36
- 239000000446 fuel Substances 0.000 description 16
- 230000001172 regenerating effect Effects 0.000 description 6
- 238000010079 rubber tapping Methods 0.000 description 4
- 238000011144 upstream manufacturing Methods 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000629264 Halicreas minimum Species 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 238000006073 displacement reaction Methods 0.000 description 2
- 239000002803 fossil fuel Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Classifications
-
- 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
- F01K3/00—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein
- F01K3/18—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having heaters
- F01K3/20—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having heaters with heating by combustion gases of main boiler
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
- F25J3/04012—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of warm gaseous streams; details of intake or interstage cooling
- F25J3/04018—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of warm gaseous streams; details of intake or interstage cooling of main feed air
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
- F25J3/04109—Arrangements of compressors and /or their drivers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
- F25J3/04109—Arrangements of compressors and /or their drivers
- F25J3/04115—Arrangements of compressors and /or their drivers characterised by the type of prime driver, e.g. hot gas expander
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
- F25J3/04109—Arrangements of compressors and /or their drivers
- F25J3/04115—Arrangements of compressors and /or their drivers characterised by the type of prime driver, e.g. hot gas expander
- F25J3/04121—Steam turbine as the prime mechanical driver
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
- F25J3/04109—Arrangements of compressors and /or their drivers
- F25J3/04115—Arrangements of compressors and /or their drivers characterised by the type of prime driver, e.g. hot gas expander
- F25J3/04133—Electrical motor as the prime mechanical driver
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
- F25J3/04109—Arrangements of compressors and /or their drivers
- F25J3/04139—Combination of different types of drivers mechanically coupled to the same compressor, possibly split on multiple compressor casings
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04521—Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
- F25J3/04527—Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general
- F25J3/04533—Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the direct combustion of fuels in a power plant, so-called "oxyfuel combustion"
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04521—Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
- F25J3/04593—The air gas consuming unit is also fed by an air stream
- F25J3/046—Completely integrated air feed compression, i.e. common MAC
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04521—Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
- F25J3/04612—Heat exchange integration with process streams, e.g. from the air gas consuming unit
- F25J3/04618—Heat exchange integration with process streams, e.g. from the air gas consuming unit for cooling an air stream fed to the air fractionation unit
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04763—Start-up or control of the process; Details of the apparatus used
- F25J3/04866—Construction and layout of air fractionation equipments, e.g. valves, machines
- F25J3/04969—Retrofitting or revamping of an existing air fractionation unit
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2230/00—Processes or apparatus involving steps for increasing the pressure of gaseous process streams
- F25J2230/04—Compressor cooling arrangement, e.g. inter- or after-stage cooling or condensate removal
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2230/00—Processes or apparatus involving steps for increasing the pressure of gaseous process streams
- F25J2230/80—Processes or apparatus involving steps for increasing the pressure of gaseous process streams the fluid being carbon dioxide
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2240/00—Processes or apparatus involving steps for expanding of process streams
- F25J2240/70—Steam turbine, e.g. used in a Rankine cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2260/00—Coupling of processes or apparatus to other units; Integrated schemes
- F25J2260/80—Integration in an installation using carbon dioxide, e.g. for EOR, sequestration, refrigeration etc.
-
- 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
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Definitions
- the invention relates to a steam generating plant with the features of the preamble of claim 1 and a method for operating or retrofitting a steam generator plant according to claim 17 or claim 23.
- Such steam generators produce CO 2 due to the combustion of the fossil fuel, which is responsible for the destruction of the ozone layer in the atmosphere.
- the industry and universities are therefore initiating joint developments in the field of power plants for the separation of CO 2 from the flue gas.
- the invention is based on the object, a generic
- the inventive retrofitting to the oxy-fuel process in the steam generation plant is included and used the reheating.
- the circuit of the steam generating plant is selected on the combustion air side so that operation with air as sole oxygen carrier continues to be possible without restriction.
- the retrofit to an oxy-fuel plant is thus carried out without affecting the conventional steam generating plant in the possible fresh air mode. Scaling to larger units is possible.
- Fig. 1 shows the circuit diagram of a steam generating plant with a
- the steam generating plant comprises a steam generator 1 with a water-steam cycle, a steam turbine set 2 and an air supply, a flue gas discharge and a regenerative air preheater heated by flue gas (combustion air pre-heater) 3.
- a steam generator 1 with a water-steam cycle a steam turbine set 2 and an air supply
- a flue gas discharge a regenerative air preheater heated by flue gas (combustion air pre-heater) 3.
- flue gas combustion air pre-heater
- the steam turbine set 2 consists of a high-pressure part 4, a medium-pressure part 5 and a low-pressure part 6, which are arranged on a common shaft and drive a generator 7 for generating electrical energy.
- the illustrated steam generator 1 is designed as a forced circulation steam generator. The following description is also applicable to a drum boiler.
- the steam generator 1 has a combustion chamber 8, which is provided with a furnace operated with gaseous fuel firing. Basically, the operation on a coal basis, taking into account a flue gas cleaning is possible.
- the evaporator heating surfaces of the combustion chamber 8 is followed by a superheater 9.
- a subsequent to the superheater 9 high pressure steam line 10 is guided to the high pressure part 4 of the steam turbine set 2.
- the Abdampfaustritt the high pressure part 4 is connected via a connecting line 11 with a reheater 12 of the steam generator 1.
- the reheater 12 is connected on the outlet side via an intermediate steam line 13 to the central pressure part 5 of the steam turbine set 2.
- the medium-pressure part 5 is the low-pressure part 6 downstream of the steam side.
- the Abdampfaustritt the low pressure part 6 is guided to a condenser 14.
- a condensate line 15 is connected, in which a condensate pump 15 'is located.
- the last Hochdruckspeisewaservor Suiter 19 ' is connected to an additional and flue gas heated feedwater or the evaporator of the steam generator 1.
- the feedwater preheaters 16, 19 are heated by bleed steam of the high-pressure part 4, the medium-pressure part 5 and the low-pressure part 6 of the steam turbine set 2.
- a blower 20 is disposed in an air supply pipe 21 which is connected to the inlet side air part of the regenerative air preheater 3 and guided downstream of the air preheater 3 to the furnace 8 to supply it with combustion air.
- a flue gas line 22 is connected, which is guided to the input-side gas part of the regenerative air preheater 3.
- the flue gas duct 22 is shown interrupted at the points "b" in the drawing, following the air preheater 3, the flue gas duct 22 is led to a chimney 36.
- an air line 23 is branched off and led to an air compressor 24.
- the outlet of the air compressor 24 is guided to an air separation plant 25.
- the oxygen outlet of the air separation plant 25 is connected via an oxygen line 26 to a gas mixer 27, which is arranged in the air supply line 21 between the air preheater 3 and the firing of the combustion chamber 8 of the steam generator 1.
- the air compressor 24 is driven by a drive steam turbine 28.
- the drive steam turbine 28 is acted upon in accordance with FIG. 1 with steam, which is taken from the intermediate steam line 13 between the reheater 12 of the steam generator 1 and the medium-pressure part 5 of the steam turbine set 2 via a steam line 29.
- the steam line 29 is shown interrupted at the points "a" in the drawing
- a control valve 30 is arranged in the steam line 29.
- the exhaust steam outlet of the drive steam turbine 28 is led to a condenser 31 which overflows a condensate line 32, in a pump 33 is arranged, with the condensate line 15 of the steam generator 1 upstream of the first
- Low pressure feedwater pre-heater of the low pressure feedwater preheater group 16 is connected.
- the exhaust steam of the drive steam turbine 28 can be fed to the main condenser 14 of the steam generator 1.
- the capacitor 31 of the drive steam turbine 28 and the associated condensate pump 33 can be omitted.
- a drive steam turbine 28 ' is shown, which is not acted upon by intermediate steam but with bleed steam.
- the tapping steam is removed at a suitable tapping stage 47 of the steam turbine set 2 and fed via a steam line 29 'of the drive steam turbine 28'.
- a drive steam turbine 28 " which is supplied with steam from an external steam source 48 via a steam line 29".
- This external source of steam may be a direct fired steam generator.
- two air cooler 34, 35 are arranged in the air line 23 between the air preheater 3 and the air compressor 24 in the air line 23 between the air preheater 3 and the air compressor 24.
- the air coolers 34, 35 are integrated into the water-steam cycle of the steam generator 1 as the drive steam turbine 28 driving the air compressor 24.
- the air cooler 34 located upstream of the air preheater 3 is flowed through by high-pressure feed water, which flows downstream of the condensate line 15
- a recirculation fan 37 is arranged downstream of the flue gas duct 22 downstream of the regenerative air preheater 3 and a branch to a chimney 36. Downstream of
- the flue gas duct 22 branches into two flue gas side lines 38, 39.
- the first flue gas secondary line 38 opens into the gas mixer 27th
- the second flue gas secondary line 39 is led to a C0 2 compressor 40.
- the C0 2 compressor 40 is driven by an expander 42 and a motor / generator 41.
- the C0 2 compressor 40 and the expander 42 are arranged together with the motor / generator 41 on a shaft.
- the motor / generator 41 can also be dispensed with. Instead, the air compressor 24, the expander 42 and the C0 2 compressor 40 are arranged together with the drive steam turbine 28 "or the electric motor 49 as drive means on a single-shaft train 50. It should be emphasized that the drive train shown in FIGS. 3 and 4 can also be used in a steam generator system according to FIGS. 1 and 2, as well as the drive train according to FIGS. 1 and 2 in a steam generator system according to FIGS 4 is possible.
- heat exchanger 43 are arranged to cool the flue gas below the water dew point before entering the C0 2 compressor, whereby the separation of water from the flue gas.
- the heat exchangers 43 are connected to the expander 42 via a connecting line 44 'by a Rankine Circuit 44 connected in the working medium as a refrigerant with a low boiling temperature, eg. B. NH 3 is used.
- a connected to the output of the expander 42 pump 45 provides for the circulation of the working fluid through the heat exchanger 43 and the expander 42nd
- the leading via the air compressor 24 to the air separation unit 25 and the air cooler 34, 35 receiving air line 23 and outgoing from the air separation unit 25 oxygen line 26 are connected in parallel to the leading to the combustion chamber 8 air supply line 21.
- Flue gas secondary line 38 and the second flue gas secondary line 39 provide for shutting off the relevant line or for regulating the medium flowing through the relevant line.
- the steam generating plant described above is operated as follows.
- the air required for the oxy-fuel process ie for operation with oxygen, is cooled behind the regenerative air preheater 3 by means of steam turbine condensate to the lowest possible temperatures and compressed in the air compressor 24 to the pressure necessary for the air separation plant 25.
- the drive of the air compressor 24 by means of the drive steam turbine 28, 28 ' which is fed with intermediate steam from the reheater 12 or with bleed steam from the tap 47 of the medium-pressure part 5 of the steam turbine 2.
- the reduced power of the steam turbine set 2 is small because the removal of the intermediate or bleed steam is quantitatively partially compensated by the displacement of the heat of the combustion air in the condensate circuit of the steam generator 1 by the tapping points of the steam lines on the medium-pressure and low-pressure side closed or only are partially open.
- the resulting condensate of the drive steam turbine 28, 28 ' is integrated into the condensate circuit of the steam generator 1. As a result, no additional degasser and no additional steam condensate system necessary.
- the absorption capacity of the steam turbine set 2 is sufficient and the generator 7 still has additional reserves, then one could decouple the drive of the air compressor 24 from the intermediate steam rail, consisting of intermediate steam line 13 and tapping stage 47, of the medium-pressure part 5 of the steam turbine set 2.
- Both an electric motor and a pure steam turbine process with a directly fired steam generator are available for this purpose.
- the advantage of such concepts lies in the latter both in the free choice of steam parameters and in the improved dynamics of the switching process of the steam generating plant to pure air operation, in the case of a trip of the additional turbomachinery for the oxy-fuel process.
- the intermediate and aftercooler heat of the air compressor 24 could be usefully integrated into the retrofit plant concept.
- the air for the air separation plant 25 is compressed by the air compressor 24 to the necessary pressure for the air separation plant 25.
- the combination of axial and radial compressors with intermediate and aftercoolers is ideal. Basically, a purely motorized drive is possible.
- the startup of the steam generating plant is carried out with 100% load of the blower 20, wherein about 60% of the air separation plant 25, d.
- the values given may vary according to the method.
- the steam generator 1 runs in the partial load fresh air operation until the corresponding O 2 quality is achieved in the air separation plant 25. Then the switchover takes place on oxy-fuel operation from part-load air mode to the corresponding part-load oxygen mode. Further increases in load then take place taking into account the permissible values of the air separation plant 25. The transition from oxygen to air operation then takes place in the reverse direction.
- the flue gas mass flows in the flue gas path of the steam generator 1 accordingly while significantly increasing the firing temperatures.
- the increase in the firing temperatures would lead to significant heat loads on the tubes in the combustion chamber 8 of the steam generator 1.
- both the mass flows and the combustion temperatures are adjusted to similar values as in the fresh air mode.
- shut-off / control valves 46 are arranged in the air supply line 21, the air line 23, the oxygen line 26, the first flue gas secondary line 38 and the second flue gas secondary line 39.
- the oxy-fuel process is integrated into the steam generating plant 1, that at any time a pure fresh air operation without oxygen supply is possible.
- the corresponding shut-off / control valves 46 are to close.
- a pure fresh air operation of the steam generating plant 1 is also possible in case of failure or shutdown of turbomachinery such as air compressor 24, expander 42 and C0 2 compressor 40.
- a short circuit after completion of the parallel connected, belonging to the oxy-fuel process plant components takes place during the inspection time of the steam generator system.
- the remaining flue gases consisting mainly of CO 2 and H 2 O, are cooled to remove the water content via the Rankine cycle process 44 on NH 3 basis far below the water dew point of the flue gas. Due to the released heat of vaporization of the water vapor content and the latent heat of the flue gases, additional electrical energy can be obtained via the expander 42.
- the expander 42 drives via the motor / generator 41 to the C0 2 compressor 40, which supplies the required predetermined CO 2 end pressures depending on the intended use. In this case, a compression to 200 bar for an EOR process (Enhanced Oil Recovering Process) can be achieved. Depending on the required drive power of the compressor 40 is either motor or generator operation.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
- Air Supply (AREA)
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/921,811 US7861526B2 (en) | 2005-06-08 | 2006-06-03 | Steam generation plant and method for operation and retrofitting of a steam generation plant |
BRPI0611664-7A BRPI0611664A2 (pt) | 2005-06-08 | 2006-06-03 | unidade geradora de vapor e processo para operar e reequipar uma instalação geradora de vapor |
CA002611185A CA2611185A1 (en) | 2005-06-08 | 2006-06-03 | Steam generation plant and method for operation and retrofitting of a steam generation plant |
EP06754116A EP1893848A2 (de) | 2005-06-08 | 2006-06-03 | Dampferzeugungsanlage und verfahren zum betreiben und nachrüsten einer dampferzeuganlage |
JP2008515115A JP2008545945A (ja) | 2005-06-08 | 2006-06-03 | 蒸気発生設備および蒸気発生設備の運転方法とその追加装備方法 |
CN2006800200232A CN101203660B (zh) | 2005-06-08 | 2006-06-03 | 蒸汽发生设备以及用于运行和改装蒸汽发生设备的方法 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102005026534A DE102005026534B4 (de) | 2005-06-08 | 2005-06-08 | Dampferzeugungsanlage |
DE102005026534.0 | 2005-06-08 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2006131283A2 true WO2006131283A2 (de) | 2006-12-14 |
WO2006131283A3 WO2006131283A3 (de) | 2007-04-26 |
Family
ID=37498798
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2006/005334 WO2006131283A2 (de) | 2005-06-08 | 2006-06-03 | Dampferzeugungsanlage und verfahren zum betreiben und nachrüsten einer dampferzeuganlage |
Country Status (9)
Country | Link |
---|---|
US (1) | US7861526B2 (de) |
EP (1) | EP1893848A2 (de) |
JP (1) | JP2008545945A (de) |
CN (1) | CN101203660B (de) |
BR (1) | BRPI0611664A2 (de) |
CA (1) | CA2611185A1 (de) |
DE (1) | DE102005026534B4 (de) |
RU (1) | RU2380548C2 (de) |
WO (1) | WO2006131283A2 (de) |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008149284A2 (en) * | 2007-06-08 | 2008-12-11 | Foster Wheeler Energy Corporation | Method of and power plant for generating power by oxyfuel combustion |
FR2927654A1 (fr) * | 2008-02-18 | 2009-08-21 | L'air Liquide Sa Pour L'edtude Et L'exloitation Des Procedes Georges Claude | Integration d'un appareil de separation d'air et d'un cycle a rechauffage de vapeur |
WO2009103926A2 (fr) * | 2008-02-18 | 2009-08-27 | L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Intégration d'un appareil de séparation d'air et d'un cycle à réchauffage de vapeur |
WO2009130660A2 (en) * | 2008-04-22 | 2009-10-29 | Foster Wheeler Energy Corporation | Oxyfuel combusting boiler system and a method of generating power by using the boiler system |
WO2009144366A2 (en) * | 2008-05-30 | 2009-12-03 | Foster Wheeler Energia Oy | Method of and system for generating power by oxyfuel combustion |
WO2009144369A2 (en) * | 2008-05-30 | 2009-12-03 | Foster Wheeler Energia Oy | Method of and system for generating power by oxyfuel combustion |
FR2938320A1 (fr) * | 2008-11-10 | 2010-05-14 | Air Liquide | Installation integree de separation d'air et de chauffage d'eau destinee a une chaudiere |
EP2212621A2 (de) * | 2007-11-26 | 2010-08-04 | L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude | Anpassung einer oxyfuel-verbrennungsanlage an die verfügbare elektrische energie und an die menge des zu erzeugenden co2 |
CN102047061A (zh) * | 2008-05-30 | 2011-05-04 | 福斯特韦勒能源股份公司 | 通过氧化燃料燃烧发电的方法和系统 |
US8528342B2 (en) | 2009-03-23 | 2013-09-10 | Man Diesel & Turbo Se | Power plant for IGSC-process |
WO2013160161A3 (de) * | 2012-04-26 | 2014-10-23 | Siemens Aktiengesellschaft | Niedertemperatur-kreislauf für eine gas- und dampfturbinenanlage mit wasserstofffeuerung |
EP2942496A1 (de) * | 2014-05-08 | 2015-11-11 | Alstom Technology Ltd | Oxy-Heizkessel-Kraftwerk mit einer wärmeintegrierten Lufttrennungseinheit |
RU2572472C2 (ru) * | 2012-05-29 | 2016-01-10 | Владимир Петрович Толстоухов | Плазменная котельная установка |
Families Citing this family (30)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8196532B2 (en) * | 2008-02-27 | 2012-06-12 | Andrus Jr Herbert E | Air-fired CO2 capture ready circulating fluidized bed heat generation with a reactor subsystem |
US8146363B2 (en) * | 2009-02-06 | 2012-04-03 | Siemens Energy, Inc. | Condenser system |
CN101893165B (zh) * | 2009-05-21 | 2013-03-13 | 西安同大实业有限公司 | 中高压工艺流体高位能综合利用系统 |
EP2305964A1 (de) * | 2009-09-23 | 2011-04-06 | Siemens Aktiengesellschaft | Dampfkraftwerk |
FR2957408B1 (fr) * | 2010-03-09 | 2015-07-17 | Air Liquide | Procede et appareil de chauffage d'un gaz de l'air provenant d'un appareil de separation d'air |
CN101893252A (zh) * | 2010-07-18 | 2010-11-24 | 赵军政 | 高效节能环保的火力发电机组 |
JP5832103B2 (ja) * | 2011-02-25 | 2015-12-16 | 三菱重工業株式会社 | ボイラプラント |
EP2551477A1 (de) * | 2011-07-29 | 2013-01-30 | Siemens Aktiengesellschaft | Verfahren und fossilbefeuerte Kraftwerksanlage zur Rückgewinnung eines Kondensats |
CN103104303A (zh) * | 2012-10-24 | 2013-05-15 | 云南丰普科技有限公司 | 一种汽轮机抽汽量可调的汽轮机抽汽系统 |
JP6109577B2 (ja) * | 2013-01-08 | 2017-04-05 | 一般財団法人電力中央研究所 | 水素焚ガスタービンコンバインドサイクル発電プラント |
CN103133069B (zh) * | 2013-01-27 | 2015-06-10 | 南京瑞柯徕姆环保科技有限公司 | 蒸汽朗肯-氨蒸汽朗肯联合循环发电装置 |
CN103089352B (zh) * | 2013-01-27 | 2015-05-06 | 南京瑞柯徕姆环保科技有限公司 | 混合式蒸汽朗肯联合循环发电装置 |
CN103133070B (zh) * | 2013-01-27 | 2015-03-04 | 南京瑞柯徕姆环保科技有限公司 | 蒸汽朗肯-低沸点工质朗肯联合循环发电装置 |
DE102013210430B4 (de) * | 2013-06-05 | 2015-07-09 | Siemens Aktiengesellschaft | Energiespeichervorrichtung zur Vorwärmung von Speisewasser |
CA2929346A1 (en) * | 2013-11-07 | 2015-05-14 | Sasol Technology Proprietary Limited | Method and plant for co-generation of heat and power |
EP2942495B1 (de) * | 2014-05-08 | 2018-10-10 | General Electric Technology GmbH | Kohlebefeuerte Oxy-Anlage mit Wärmeintegration |
EP2942494B1 (de) * | 2014-05-08 | 2019-08-21 | General Electric Technology GmbH | Kohlebefeuerte Oxy-Anlage mit Wärmeintegration |
EP2942497B1 (de) * | 2014-05-08 | 2018-10-31 | General Electric Technology GmbH | Oxy-Boiler-Kraftwerk mit Wärmeintegration des Sauerstoffzufuhrsystems |
DE102015218502A1 (de) | 2015-09-25 | 2017-03-30 | Siemens Aktiengesellschaft | Dampfturbinenkraftwerk mit Wasserstoffverbrennung unter Einbindung einer Vergasungseinrichtung |
CN105649690B (zh) * | 2015-12-29 | 2017-03-15 | 西安交通大学 | 一种大热电比热电联产系统及其工作方法 |
CA3012359A1 (en) * | 2016-02-29 | 2017-09-08 | XDI Holdings, LLC | Improved dirty water and exhaust constituent free, direct steam generation, convaporator system, apparatus and method |
CN106677838B (zh) * | 2016-12-29 | 2018-04-13 | 江苏河海新能源股份有限公司 | 一种燃气蒸汽联合循环发电装置及方法 |
CN106801654B (zh) * | 2016-12-29 | 2019-10-22 | 江苏河海新能源股份有限公司 | 一种热力压水堆循环发电装置 |
IT201700074290A1 (it) * | 2017-07-03 | 2019-01-03 | Ivar Spa | Macchina termica configurata per realizzare cicli termici e metodo per realizzare cicli termici mediante tale macchina termica |
EP3438584B1 (de) * | 2017-08-03 | 2020-03-11 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Verfahren und gerät zur trennung von luft durch kryogene destillation |
RU2702206C1 (ru) * | 2018-06-13 | 2019-10-04 | Михаил Аркадьевич Верткин | Котлотурбинная диоксид-углеродная энергоустановка |
FR3086694B1 (fr) * | 2018-10-02 | 2023-12-22 | Entent | Machine de conversion de chaleur fatale en energie mecanique |
US11396789B2 (en) | 2020-07-28 | 2022-07-26 | Saudi Arabian Oil Company | Isolating a wellbore with a wellbore isolation system |
US11136868B1 (en) | 2020-09-03 | 2021-10-05 | Saudi Arabian Oil Company | Aqueous flash treatment in well applications |
US11624265B1 (en) | 2021-11-12 | 2023-04-11 | Saudi Arabian Oil Company | Cutting pipes in wellbores using downhole autonomous jet cutting tools |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4545787A (en) * | 1984-07-30 | 1985-10-08 | Air Products And Chemicals, Inc. | Process for producing by-product oxygen from turbine power generation |
WO2003040531A1 (fr) * | 2001-11-09 | 2003-05-15 | Kawasaki Jukogyo Kabushiki Kaisha | Systeme de turbine a gaz comprenant un systeme ferme entre le gaz combustible et le gaz de combustion au moyen d'une couche de charbon souterraine |
US20030131582A1 (en) * | 2001-12-03 | 2003-07-17 | Anderson Roger E. | Coal and syngas fueled power generation systems featuring zero atmospheric emissions |
WO2003069132A1 (en) * | 2002-02-11 | 2003-08-21 | L'air Liquide, Societe Anonyme A Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude | Integrated air separation and oxygen fired power generation system |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3926964A1 (de) * | 1989-08-16 | 1991-02-21 | Siemens Ag | Verfahren zur minderung des kohlendioxidgehalts des abgases eines gas- und dampfturbinenkraftwerks und danach arbeitendes kraftwerk |
DE4117192C2 (de) * | 1991-05-25 | 1994-06-23 | Saarbergwerke Ag | Verfahren zur Erzeugung von Energie in einer kombinierten Gas-Dampfkraftanlage und Anlage zur Durchführung des Verfahrens |
JP3007200B2 (ja) * | 1991-09-09 | 2000-02-07 | 川崎重工業株式会社 | 燃焼ガスの処理方法及び装置 |
US5623822A (en) * | 1995-05-23 | 1997-04-29 | Montenay International Corp. | Method of operating a waste-to-energy plant having a waste boiler and gas turbine cycle |
JP3771606B2 (ja) * | 1995-07-21 | 2006-04-26 | 三菱重工業株式会社 | ガスタービン排気再燃複合プラント |
DE59711190D1 (de) * | 1997-11-19 | 2004-02-12 | Alstom Switzerland Ltd | Verfahren und Vorrichtung zur Brennstoffvorwärmung einer Feuerungsanlage |
US5979183A (en) * | 1998-05-22 | 1999-11-09 | Air Products And Chemicals, Inc. | High availability gas turbine drive for an air separation unit |
DE19832293A1 (de) * | 1998-07-17 | 1999-10-21 | Siemens Ag | Gas- und Dampfturbinenanlage |
JP4725985B2 (ja) * | 2000-03-03 | 2011-07-13 | バブコック日立株式会社 | 排煙処理装置の運転方法 |
US6637183B2 (en) * | 2000-05-12 | 2003-10-28 | Clean Energy Systems, Inc. | Semi-closed brayton cycle gas turbine power systems |
WO2002095852A2 (en) * | 2001-05-24 | 2002-11-28 | Clean Energy Systems, Inc. | Combined fuel cell and fuel combustion power generation systems |
US6709573B2 (en) * | 2002-07-12 | 2004-03-23 | Anthon L. Smith | Process for the recovery of hydrocarbon fractions from hydrocarbonaceous solids |
AU2003295610B2 (en) * | 2002-11-15 | 2010-01-28 | Clean Energy Systems, Inc. | Low pollution power generation system with ion transfer membrane air separation |
-
2005
- 2005-06-08 DE DE102005026534A patent/DE102005026534B4/de not_active Expired - Fee Related
-
2006
- 2006-06-03 JP JP2008515115A patent/JP2008545945A/ja active Pending
- 2006-06-03 CA CA002611185A patent/CA2611185A1/en not_active Abandoned
- 2006-06-03 CN CN2006800200232A patent/CN101203660B/zh not_active Expired - Fee Related
- 2006-06-03 RU RU2007149248/06A patent/RU2380548C2/ru not_active IP Right Cessation
- 2006-06-03 WO PCT/EP2006/005334 patent/WO2006131283A2/de active Application Filing
- 2006-06-03 BR BRPI0611664-7A patent/BRPI0611664A2/pt not_active IP Right Cessation
- 2006-06-03 EP EP06754116A patent/EP1893848A2/de not_active Withdrawn
- 2006-06-03 US US11/921,811 patent/US7861526B2/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4545787A (en) * | 1984-07-30 | 1985-10-08 | Air Products And Chemicals, Inc. | Process for producing by-product oxygen from turbine power generation |
WO2003040531A1 (fr) * | 2001-11-09 | 2003-05-15 | Kawasaki Jukogyo Kabushiki Kaisha | Systeme de turbine a gaz comprenant un systeme ferme entre le gaz combustible et le gaz de combustion au moyen d'une couche de charbon souterraine |
US20030131582A1 (en) * | 2001-12-03 | 2003-07-17 | Anderson Roger E. | Coal and syngas fueled power generation systems featuring zero atmospheric emissions |
WO2003069132A1 (en) * | 2002-02-11 | 2003-08-21 | L'air Liquide, Societe Anonyme A Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude | Integrated air separation and oxygen fired power generation system |
Non-Patent Citations (1)
Title |
---|
STICHER W ET AL: "WIRKUNGSGRADOPTIMIERTES INDUSTRIEKRAFTWERK MIT HOCHOFENGASFEUERUNG BLAST FURNACE GAS-FIRED INDUSTRIAL POWER PLANT WITH IMPROVED EFFICIENCY" VGB POWERTECH, VGB POWERTECH, ESSEN, DE, Bd. 83, Nr. 12, 2003, Seiten 68-70,72, XP001047232 ISSN: 1435-3199 * |
Cited By (29)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7874140B2 (en) | 2007-06-08 | 2011-01-25 | Foster Wheeler North America Corp. | Method of and power plant for generating power by oxyfuel combustion |
WO2008149284A3 (en) * | 2007-06-08 | 2009-11-26 | Foster Wheeler Energy Corporation | Method of and power plant for generating power by oxyfuel combustion |
WO2008149284A2 (en) * | 2007-06-08 | 2008-12-11 | Foster Wheeler Energy Corporation | Method of and power plant for generating power by oxyfuel combustion |
EP2212621A2 (de) * | 2007-11-26 | 2010-08-04 | L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude | Anpassung einer oxyfuel-verbrennungsanlage an die verfügbare elektrische energie und an die menge des zu erzeugenden co2 |
JP2011505537A (ja) * | 2007-11-26 | 2011-02-24 | レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード | エネルギー利用率および捕捉すべきco2量へのオキシ燃焼プラントの適応 |
FR2927654A1 (fr) * | 2008-02-18 | 2009-08-21 | L'air Liquide Sa Pour L'edtude Et L'exloitation Des Procedes Georges Claude | Integration d'un appareil de separation d'air et d'un cycle a rechauffage de vapeur |
WO2009103926A2 (fr) * | 2008-02-18 | 2009-08-27 | L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Intégration d'un appareil de séparation d'air et d'un cycle à réchauffage de vapeur |
AU2009216592B2 (en) * | 2008-02-18 | 2012-11-01 | L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Integration of an air separation apparatus and of a steam reheating cycle |
JP2011518269A (ja) * | 2008-02-18 | 2011-06-23 | レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード | 空気分離装置及び水蒸気再熱サイクルの統合 |
CN102046929A (zh) * | 2008-02-18 | 2011-05-04 | 乔治洛德方法研究和开发液化空气有限公司 | 空气分离设备和蒸汽再热循环的集成 |
WO2009103926A3 (fr) * | 2008-02-18 | 2011-03-03 | L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Intégration d'un appareil de séparation d'air et d'un cycle à réchauffage de vapeur |
AU2009239601B2 (en) * | 2008-04-22 | 2011-11-17 | Foster Wheeler Energy Corporation | Oxyfuel combusting boiler system and a method of generating power by using the boiler system |
CN102016241A (zh) * | 2008-04-22 | 2011-04-13 | 福斯特能源公司 | 氧燃料燃烧锅炉系统和使用所述锅炉系统产生动力的方法 |
WO2009130660A2 (en) * | 2008-04-22 | 2009-10-29 | Foster Wheeler Energy Corporation | Oxyfuel combusting boiler system and a method of generating power by using the boiler system |
WO2009130660A3 (en) * | 2008-04-22 | 2010-12-23 | Foster Wheeler Energy Corporation | Oxyfuel combusting boiler system and a method of generating power by using the boiler system |
WO2009144369A2 (en) * | 2008-05-30 | 2009-12-03 | Foster Wheeler Energia Oy | Method of and system for generating power by oxyfuel combustion |
WO2009144366A2 (en) * | 2008-05-30 | 2009-12-03 | Foster Wheeler Energia Oy | Method of and system for generating power by oxyfuel combustion |
CN102047061A (zh) * | 2008-05-30 | 2011-05-04 | 福斯特韦勒能源股份公司 | 通过氧化燃料燃烧发电的方法和系统 |
WO2009144369A3 (en) * | 2008-05-30 | 2010-12-16 | Foster Wheeler Energia Oy | Method of and system for generating power by oxyfuel combustion |
WO2009144366A3 (en) * | 2008-05-30 | 2011-03-03 | Foster Wheeler Energia Oy | Method of and system for generating power by oxyfuel combustion |
WO2010052437A3 (fr) * | 2008-11-10 | 2011-06-03 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Installation integree de separation d'air et de chauffage d'eau destinee a une chaudiere |
WO2010052437A2 (fr) | 2008-11-10 | 2010-05-14 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Installation integree de separation d'air et de chauffage d'eau destinee a une chaudiere |
FR2938320A1 (fr) * | 2008-11-10 | 2010-05-14 | Air Liquide | Installation integree de separation d'air et de chauffage d'eau destinee a une chaudiere |
US8528342B2 (en) | 2009-03-23 | 2013-09-10 | Man Diesel & Turbo Se | Power plant for IGSC-process |
EP2423457A3 (de) * | 2009-03-23 | 2014-01-15 | MAN Diesel & Turbo SE | Kraftwerk für IGSC-Prozess |
WO2013160161A3 (de) * | 2012-04-26 | 2014-10-23 | Siemens Aktiengesellschaft | Niedertemperatur-kreislauf für eine gas- und dampfturbinenanlage mit wasserstofffeuerung |
RU2572472C2 (ru) * | 2012-05-29 | 2016-01-10 | Владимир Петрович Толстоухов | Плазменная котельная установка |
EP2942496A1 (de) * | 2014-05-08 | 2015-11-11 | Alstom Technology Ltd | Oxy-Heizkessel-Kraftwerk mit einer wärmeintegrierten Lufttrennungseinheit |
US10001279B2 (en) | 2014-05-08 | 2018-06-19 | General Electric Technology Gmbh | Oxy boiler power plant with a heat integrated air separation unit |
Also Published As
Publication number | Publication date |
---|---|
US20100132360A1 (en) | 2010-06-03 |
CN101203660B (zh) | 2013-07-24 |
JP2008545945A (ja) | 2008-12-18 |
BRPI0611664A2 (pt) | 2012-12-04 |
RU2007149248A (ru) | 2009-07-20 |
CA2611185A1 (en) | 2006-12-14 |
DE102005026534B4 (de) | 2012-04-19 |
US7861526B2 (en) | 2011-01-04 |
DE102005026534A1 (de) | 2006-12-28 |
WO2006131283A3 (de) | 2007-04-26 |
EP1893848A2 (de) | 2008-03-05 |
CN101203660A (zh) | 2008-06-18 |
RU2380548C2 (ru) | 2010-01-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP1893848A2 (de) | Dampferzeugungsanlage und verfahren zum betreiben und nachrüsten einer dampferzeuganlage | |
EP1591644B1 (de) | Vorrichtung zur Ausnutzung der Abwärme von Verdichtern | |
DE4333439C1 (de) | Vorrichtung zur Kühlmittelkühlung einer gekühlten Gasturbine einer Gas- und Dampfturbinenanlage | |
EP0750718B1 (de) | Verfahren zum betreiben einer gas- und dampfturbinenanlage sowie danach arbeitende anlage | |
DE4434526C1 (de) | Verfahren zum Betreiben einer Gas- und Dampfturbinenanlage sowie danach arbeitende Anlage | |
EP0523467A1 (de) | Verfahren zum Betreiben einer Gas- und Dampfturbinenanlage und Anlage zur Durchführung des Verfahrens | |
EP2196633A1 (de) | Kraftwerk mit einer Turbineneinheit und einem Generator | |
DE102018123663A1 (de) | Brennstoffvorwärmsystem für eine Verbrennungsgasturbine | |
EP1866521A2 (de) | Verfahren zum starten einer gas- und dampfturbinenanlage | |
EP1119688A1 (de) | Gas- und dampfturbinenanlage | |
DE19506787A1 (de) | Verfahren zum Betrieb einer Dampfturbine | |
EP0523466B1 (de) | Verfahren zum Betreiben einer Gas- und Dampfturbinenanlage und Anlage zur Durchführung des Verfahrens | |
EP1801363A1 (de) | Kraftwerksanlage | |
EP0981681B1 (de) | Gas- und dampfturbinenanlage und verfahren zur kühlung des kühlmittels der gasturbine einer derartigen anlage | |
DE10155508C2 (de) | Verfahren und Vorrichtung zur Erzeugung von elektrischer Energie | |
DE19720789B4 (de) | Verfahren und Vorrichtung zur Erzeugung von Dampf | |
DE102012110579B4 (de) | Anlage und Verfahren zur Erzeugung von Prozessdampf | |
DE19627425A1 (de) | Verfahren zum Betrieb einer Hybrid-Solar-Kombianlage sowie eine Hybrid-Solar-Kombianlage | |
DE3224577A1 (de) | Kombinierte gasturbinen/dampfturbinenanlage | |
DE3815993A1 (de) | Zweistoff-turbinenanlage | |
DE19849740A1 (de) | Gas- und Dampfturbinenanlage | |
CH718340A2 (de) | Steigerung der Leistung von Gas- und Dampfturbinenanlagen bei einer neuen Zusatzvorfeuerung. | |
EP0915233B1 (de) | Hybridkraftwerk | |
DE102013205053B4 (de) | Verfahren zum Betrieb eines einen Wasser-Dampf-Kreislauf aufweisenden Kraftwerks | |
DE3343319A1 (de) | Kombinierte gasturbinen-dampfturbinenanlage bzw. gasturbinenanlage |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 2611185 Country of ref document: CA Ref document number: 200680020023.2 Country of ref document: CN |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2008515115 Country of ref document: JP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2098/MUMNP/2007 Country of ref document: IN |
|
REEP | Request for entry into the european phase |
Ref document number: 2006754116 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2006754116 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 11921811 Country of ref document: US |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2007149248 Country of ref document: RU |
|
WWP | Wipo information: published in national office |
Ref document number: 2006754116 Country of ref document: EP |
|
ENP | Entry into the national phase |
Ref document number: PI0611664 Country of ref document: BR Kind code of ref document: A2 Effective date: 20071207 |