US20120027627A1 - Compressor system for a process gas plant having heat return, and the process gas plant for carbon dioxide gas separation - Google Patents

Compressor system for a process gas plant having heat return, and the process gas plant for carbon dioxide gas separation Download PDF

Info

Publication number
US20120027627A1
US20120027627A1 US13/262,257 US201013262257A US2012027627A1 US 20120027627 A1 US20120027627 A1 US 20120027627A1 US 201013262257 A US201013262257 A US 201013262257A US 2012027627 A1 US2012027627 A1 US 2012027627A1
Authority
US
United States
Prior art keywords
process gas
cooler
gas cooler
compressor
coolers
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US13/262,257
Other languages
English (en)
Inventor
David Getze
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Siemens AG
Original Assignee
Siemens AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Siemens AG filed Critical Siemens AG
Assigned to SIEMENS AKTIENGESELLSCHAFT reassignment SIEMENS AKTIENGESELLSCHAFT ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: GETZE, DAVID
Publication of US20120027627A1 publication Critical patent/US20120027627A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • 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
    • B01D53/002—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 condensation
    • 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
    • F25J3/0228—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 characterised by the separated product stream
    • F25J3/0266—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 characterised by the separated product stream separation of carbon dioxide
    • 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
    • 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
    • F25J2230/06—Adiabatic compressor, i.e. without interstage cooling
    • 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
    • F25J2230/30—Compression of the feed stream
    • 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
    • F25J2260/00—Coupling of processes or apparatus to other units; Integrated schemes
    • F25J2260/02—Integration in an installation for exchanging heat, e.g. for waste heat recovery
    • 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
    • F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/44—Particular materials used, e.g. copper, steel or alloys thereof or surface treatments used, e.g. enhanced surface
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28B—STEAM OR VAPOUR CONDENSERS
    • F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
    • F28B1/02—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using water or other liquid as the cooling medium
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/26—Arrangements for connecting different sections of heat-exchange elements, e.g. of radiators
    • 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
    • Y02E20/32—Direct CO2 mitigation

Definitions

  • the invention refers to a compressor system for a process plant having heat return, and the process plant for carbon dioxide gas separation having the compressor system.
  • the compression of the carbon dioxide gas takes place in the compressor polytropically and, in proportion to the pressure ratio of the compressor, leads to a temperature increase of the carbon dioxide gas.
  • the compressor can be constructed from a multiplicity of compressor stages, wherein after the individual compressor stages the carbon dioxide gas is cooled by means of a cooler. As a result, the effort which is required for driving the compressor can be reduced.
  • Cooling water which flows through the cooler in a cooling water circuit, is conventionally used as the cooling medium, wherein heat is extracted from this for tempering the cooling water.
  • two cooling water circuits with different temperature levels are provided in the carbon dioxide gas separation plant, wherein the cooling water circuit with the higher temperature level is provided for cooling the carbon dioxide gas directly after discharging from the compressor stage.
  • industrial water for example, can be heated.
  • the cooling water circuit with the lower temperature level is then used for further cooling of the carbon dioxide gas to a required temperature level which, for example, is suitable for entry of the carbon dioxide gas into the next compressor stage.
  • the cooler conventionally has a housing which is exposed to admission of the carbon dioxide gas and in which two cooler bundles are accommodated, wherein one of the cooler bundles is connected to the one cooling water circuit and the other cooler bundle is connected to the other cooling water circuit.
  • the two cooler bundles are advantageously arranged next to each other in the housing, wherein the diameter of the housing is large.
  • the cooler bundles for construction-related reasons, have no common cross section so that an efficiency-optimized design of the cooler bundles is complicated.
  • the housing and the cooler bundles are constructed from stainless steel, as a result of which the production costs for the cooler are high.
  • the compressor system according to the invention for a process plant having heat return has a compressor for compressing moist process gas, having at least one compressor stage, and a process gas cooler unit which, for cooling the process gas, is connected downstream to the compressor stage, and has at least one first and one second process gas cooler which is operated with a cooling medium, wherein the process gas coolers have in each case an individual process gas cooler jacket, which is exposed to admission of the process gas, with a process gas cooler bundle accommodated therein and exposed to admission of the cooling medium, are connected directly one after the other on the process gas side, and are designed and can be operated with the cooling medium in such a way that from the process gas cooler which is arranged upstream on the process gas side a predetermined heat flow can be removed from the process gas, as a result of which the thermodynamic state of the process gas between the process gas coolers is located in the region of the dew point front, and the process gas can be cooled to a predetermined temperature by means of the process gas cooler which is arranged downstream.
  • the process gas bundles are accommodated in separate process gas cooler jackets so that the process gas coolers are thermodynamically decoupled from each other.
  • each process gas cooler can be advantageously individually designed with regard to its choice of material and its geometry, especially taking into account a diameter of the process gas cooler jackets which is as small as possible. A lower production cost and a reduced material consumption for the process gas coolers result from this.
  • the process gas is carbon dioxide
  • the materials for the process gas cooler bundles and for the process gas cooler jackets are to be selected as being corrosion-resistant.
  • stainless steel could come into consideration as corrosion-resistant material.
  • a construction of the process gas coolers with stainless steel leads to increased production costs so that the separation of the process gas coolers according to the invention is especially advantageous.
  • different materials can be used for the individual process gas jackets and the individual process gas coolers and are optimally selected with regard to corrosion-resistance, strength, thermal conductivity and costs.
  • process gas coolers can be individually designed in such a way that an optimized flow distribution can be established in the process gas cooler bundles, wherein the narrowest cross section in the process gas cooler jackets is large. As a result, pressure losses in the process gas coolers are advantageously reduced.
  • the process gas cooler which is arranged downstream is preferably equipped for removing the heat of condensation of the water which precipitates from the process gas and for separating out this water.
  • the thermodynamic state of the process gas between the process gas coolers is located just ahead of the dew point front.
  • the process gas coolers, by their process gas cooler jackets, are preferably interconnected by two transfer pipes for the parallel conducting of process gas from the process gas cooler which is arranged upstream on the process gas side to the process gas cooler which is arranged downstream.
  • at least one of the transfer pipes is preferably equipped with a compensator.
  • At least one of the process gas cooler bundles is preferably arranged eccentrically in its process gas cooler jacket.
  • at least one of the process gas cooler bundles is of a square-shaped construction and the process gas cooler jacket is of a hollow-cylindrical construction, and that the process gas cooler bundle is arranged in a tilted manner around the longitudinal axis of the process gas cooler jacket for the process gas inflow and/or for the process gas outflow in the process gas cooler jacket.
  • the process gas plant according to the invention for carbon dioxide gas separation having the compressor system has a first cooling medium circuit which is equipped for operating the process gas cooler which is arranged upstream on the process gas side, and a second cooling medium circuit which is equipped for operating the process gas cooler which is arranged downstream, wherein the process gas is moist carbon dioxide and the first cooling-medium circuit can be used for re-feeding heat into the process gas plant.
  • the process gas which discharges from the compressor stage, is cooled by the process gas cooler which is arranged upstream on the process gas side. Due to the fact that this process gas has achieved its maximum temperature directly after discharging from the compressor stage, the first cooling-medium circuit can advantageously be operated at a high temperature level. As a result, the re-feeding of heat can also take place at a high temperature level, as a result of which the re-feeding of heat is efficient.
  • the re-feeding of heat can be used for heating a consumer water circuit, for example.
  • Cooling water is preferably the cooling medium.
  • the temperature of the cooling water in the first cooling water circuit, in the inflow to the process gas cooler which is arranged upstream on the process gas side, the temperature of the cooling water is 40° C., and in the outflow from the process gas cooler which is arranged upstream on the process gas side, the temperature of the cooling water is from 120° C. to 160° C., wherein the temperature of the process gas at the process gas inlet of the process gas cooler which is arranged upstream on the process gas side is between 140° C. and 175° C.
  • the temperature of the cooling water in the inflow to the process gas cooler which is arranged downstream on the process gas side, the temperature of the cooling water is 24° C.
  • the temperature of the cooling water is 32° C., wherein the temperature of the process gas at the process gas outlet of the process gas cooler which is arranged downstream on the process gas side is 34° C.
  • FIG. 1 shows a schematic view of the embodiment of the compressor system
  • FIG. 2 shows a perspective view of the embodiment of the process gas cooler
  • FIG. 3 shows a cross-sectional view of the embodiment of the process gas cooler from FIG. 2 .
  • a compressor system 1 has a compressor 2 which is provided for compressing process gas in a process gas plant, wherein the process gas is moist carbon dioxide.
  • the process gas enters the compressor 2 via a compressor inlet 3 , is subjected to compression and, in a compressed state, discharges from the compressor 2 at a compressor exit 4 .
  • the compressor 2 is constructed as a multistage compressor and has a first up to a sixth compressor stage 5 to 10 .
  • a first process gas cooler unit 11 is provided between the second compressor stage 6 and the third compressor stage 7
  • a second process gas cooler unit 12 is provided between the fourth compressor stage 8 and the fifth compressor stage 9
  • a third process gas cooler unit 13 is provided downstream of the sixth compressor stage 10 and upstream of the compressor exit 4 . Therefore, the corresponding process gas cooler unit 11 and 12 and 13 is provided after two compressor stages 5 , 6 and 7 , 8 and 9 , 10 respectively.
  • the process gas cooler units 11 , 12 , 13 are formed in each case from two process gas coolers 14 to 19 which are exposed to throughflow by the process gas one after the other.
  • the process gas coolers 14 to 19 have in each case an individual process gas cooler jacket 34 , which is exposed to admission of the process gas, and a process gas cooler bundle 35 which is accommodated therein and exposed to admission of cooling water.
  • the process gas cooler bundles 35 of the process gas coolers 14 , 16 , 18 which are arranged upstream on the process gas side are integrated in a first cooling water circuit 28 and the process gas cooler bundles 35 of the process gas coolers 15 , 17 , 19 which are arranged downstream on the process gas side are integrated in a second cooling water circuit 31 .
  • the first cooling water circuit 28 is formed from an outflow line 29 , by which cooling water from the process gas cooler bundles 35 of the process gas coolers 14 , 16 , 18 is discharged, and an inflow line 30 , with which cooling water is directed to the process gas cooler bundles 35 of the process gas coolers 14 , 16 , 18 .
  • the second cooling water circuit 31 is formed from an outflow line 32 , from which cooling water from the process gas cooler bundles 35 of the process gas coolers 15 , 17 , 19 is discharged, and an inflow line 33 , with which cooling water is directed to the process gas cooler bundles 35 of the process gas coolers 15 , 17 , 19 .
  • the temperature level of the cooling water in the first cooling water circuit 28 is higher than the temperature level of the cooling water in the second cooling water circuit 31 , wherein the temperature of the cooling water in the inflow line 30 of the first cooling water circuit 29 is 40° C. and the temperature of the cooling water in the inflow line 33 of the second cooling water circuit 31 is 24° C.
  • the process gas at the exit of the second compressor stage 6 and therefore at the inlet 20 of the first process gas cooler 14 of the first process gas cooler unit 11 has a temperature of 175° C.
  • at the exit of the fourth compressor stage 8 and therefore at the inlet 23 of the first process gas cooler 16 of the second process gas cooler unit 12 has a temperature of 149° C.
  • at the exit of the sixth compressor stage 10 and therefore at the inlet 26 of the first process gas cooler 18 of the third process gas cooler unit 13 has a temperature of 140° C.
  • the first process gas cooler 14 of the first process gas cooler unit 11 just as the first process gas cooler 16 of the second process gas cooler unit 12 and the first process gas cooler 18 of the third process gas cooler unit 13 , are designed in such a way that a heat flow is removed from the process gas, as a result of which the thermodynamic state of the process gas between 21 the process gas coolers 14 , 15 , just as between 24 the process gas coolers 16 , 17 and between 27 the process gas coolers 18 , 19 , is located in the region of the dew point front.
  • the process gas cooler 15 of the first process gas cooler unit 11 just as the second process gas cooler 17 of the second process gas cooler unit 12 and the second process gas cooler 19 of the third process gas cooler unit 13 , cools the process gas to 34° C.
  • the cooling water in the first cooling water circuit 28 in the outflow line 29 , is heated to 120° C. to 140° C. and in the second cooling water circuit 31 , in the outflow line 32 , is heated to 32° C.
  • the process gas cooler unit 12 is shown representatively for the process gas cooler units 12 , 13 and 14 .
  • the process gas cooler bundle 35 is of a square-shaped design and arranged in the hollow-cylindrical process gas cooler jacket 34 .
  • the longitudinal center axis of the process gas cooler jacket 34 is arranged in a parallel offset manner from the longitudinal center axis of the process gas cooler bundle 35 so that the process gas cooler bundle 35 is arranged eccentrically in the process gas cooler jacket 34 .
  • the process gas cooler jacket 34 is arranged in a horizontally disposed manner, wherein the process gas cooler bundle 35 is arranged in a tilted manner around the longitudinal axis of the process gas cooler jacket 34 and is therefore tilted in relation to the horizontal.
  • the process gas cooler jacket 34 of the first process gas cooler 14 and the process gas cooler jacket 34 of the second process gas cooler 15 are formed with two transfer pipes 36 which foam the process gas-side transfer point 21 from the first process gas cooler 14 to the second process gas cooler 15 .
  • the transfer pipe 36 is arranged horizontally and the inlet 23 and the outlet 25 are arranged in a vertically extending manner.
  • the process gas cooler bundles 35 are arranged in a tilted manner around the longitudinal axis of the process gas cooler jacket 34 for the process gas flow through the inlet 23 , the transfer pipe 36 and the outlet 25 .

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Compressor (AREA)
US13/262,257 2009-04-01 2010-03-31 Compressor system for a process gas plant having heat return, and the process gas plant for carbon dioxide gas separation Abandoned US20120027627A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE102009015861.8 2009-04-01
DE102009015861 2009-04-01
PCT/EP2010/054272 WO2010112539A2 (de) 2009-04-01 2010-03-31 Verdichtersystem für eine prozessgasanlage mit wärmerückeinspeisung und die prozessgasanlage zur kohlenstoffdioxidgas-abscheidung

Publications (1)

Publication Number Publication Date
US20120027627A1 true US20120027627A1 (en) 2012-02-02

Family

ID=42828759

Family Applications (1)

Application Number Title Priority Date Filing Date
US13/262,257 Abandoned US20120027627A1 (en) 2009-04-01 2010-03-31 Compressor system for a process gas plant having heat return, and the process gas plant for carbon dioxide gas separation

Country Status (4)

Country Link
US (1) US20120027627A1 (de)
EP (1) EP2443322A2 (de)
CN (1) CN102575895A (de)
WO (1) WO2010112539A2 (de)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP4375602A1 (de) * 2022-11-28 2024-05-29 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Verfahren und vorrichtung zur verflüssigung und gegebenenfalls trennung von co2 durch destillation

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1943232A (en) * 1928-10-15 1934-01-09 Frick Co Method and apparatus for producing low temperature high pressure liquid carbon dioxide
US3027651A (en) * 1958-07-23 1962-04-03 Leybold Hochvakuum Anlagen Process and system for removing condensable vapors
US3760870A (en) * 1969-12-18 1973-09-25 Deggendorfer Werft Eisenbau Cooler construction for circulating controlled amounts of heat carrier from a reaction vessel
US3954430A (en) * 1974-10-30 1976-05-04 Ppg Industries, Inc. Liquefaction of chlorine by multi-stage compression and cooling
US4667734A (en) * 1982-03-09 1987-05-26 Laengle Karl Heat exchanger
US6053007A (en) * 1997-07-01 2000-04-25 Exxonmobil Upstream Research Company Process for separating a multi-component gas stream containing at least one freezable component
US7021013B1 (en) * 1999-02-11 2006-04-04 Khd Humboldt Wedag Ag Compensator for compensating thermal expansions

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0564722A (ja) * 1991-09-09 1993-03-19 Hitachi Ltd 燃焼排気ガス中の炭酸ガスの分離方法
US6035662A (en) * 1998-10-13 2000-03-14 Praxair Technology, Inc. Method and apparatus for enhancing carbon dioxide recovery
EP1521719A4 (de) * 2001-12-03 2008-01-23 Clean Energy Systems Inc Energieerzeugungssysteme mit kohle- und syngas-brennstoff ganz ohne atmosphärische emissionen
US6898936B1 (en) * 2002-12-04 2005-05-31 The United States Of America As Represented By The United States Department Of Energy Compression stripping of flue gas with energy recovery
US7645322B2 (en) * 2006-09-15 2010-01-12 Ingersoll Rand Energy Systems Corporation System and method for removing water and siloxanes from gas

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1943232A (en) * 1928-10-15 1934-01-09 Frick Co Method and apparatus for producing low temperature high pressure liquid carbon dioxide
US3027651A (en) * 1958-07-23 1962-04-03 Leybold Hochvakuum Anlagen Process and system for removing condensable vapors
US3760870A (en) * 1969-12-18 1973-09-25 Deggendorfer Werft Eisenbau Cooler construction for circulating controlled amounts of heat carrier from a reaction vessel
US3954430A (en) * 1974-10-30 1976-05-04 Ppg Industries, Inc. Liquefaction of chlorine by multi-stage compression and cooling
US4667734A (en) * 1982-03-09 1987-05-26 Laengle Karl Heat exchanger
US6053007A (en) * 1997-07-01 2000-04-25 Exxonmobil Upstream Research Company Process for separating a multi-component gas stream containing at least one freezable component
US7021013B1 (en) * 1999-02-11 2006-04-04 Khd Humboldt Wedag Ag Compensator for compensating thermal expansions

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP4375602A1 (de) * 2022-11-28 2024-05-29 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Verfahren und vorrichtung zur verflüssigung und gegebenenfalls trennung von co2 durch destillation
FR3142538A1 (fr) * 2022-11-28 2024-05-31 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Procédé et appareil de liquéfaction de CO2 ou de séparation de CO2 par distillation

Also Published As

Publication number Publication date
CN102575895A (zh) 2012-07-11
EP2443322A2 (de) 2012-04-25
WO2010112539A3 (de) 2012-06-07
WO2010112539A2 (de) 2010-10-07

Similar Documents

Publication Publication Date Title
US8424282B2 (en) Combined-cycle power plant with exhaust gas recycling and CO2 separation, and method for operating a combined cycle power plant
US8894921B2 (en) Flue gas cooling and cleaning system
CN101235729B (zh) 涡轮机内电气设备的冷却装置
JP6307076B2 (ja) 冷却回路、ガス用冷却乾燥設備、及び冷却回路を制御する方法
SE531841C2 (sv) Arrangemang och förfarande för återcirkulation av avgaser hos en förbränningsmotor
Kamali et al. Experience of design and optimization of multi-effects desalination systems in Iran
JP5724536B2 (ja) 圧縮機ユニット
US8393860B2 (en) Heat exchanger
JP2010101184A (ja) 空気圧縮装置
EP2365269A1 (de) Wärmetauscher- und Flüssigkeitstrennungsvorrichtung
KR102240006B1 (ko) 선박용 에어컴프레셔 폐열회수 시스템
US20120027627A1 (en) Compressor system for a process gas plant having heat return, and the process gas plant for carbon dioxide gas separation
US10526925B2 (en) Supercritical CO2 generation system for series recuperative type
CN101334247A (zh) 利用余热的空气冷却器
CN200941010Y (zh) 自加热式空冷凝汽器防冻不凝结气体抽出装置
CN201225851Y (zh) 利用余热的空气冷却器
US7284380B2 (en) Method for heat energy transmission
CZ307476B6 (cs) Zařízení pro využití kompresního tepla
US9702376B2 (en) Apparatus for compressing a wet gas flow
CN207838660U (zh) 一种压缩空气冷却除湿系统
WO2017050731A1 (en) Method and system for separating carbon dioxide from flue gas
CN201305609Y (zh) 一种高炉鼓风脱湿装置
Panangeang et al. Improve compressed air quality by utilizing aftercooler study case at PT Vale Indonesia Tbk
Siddiqui et al. Analysis On Cooling Water Circuit Of A Compressor House–A Case Study
CN108612676A (zh) 热能回收系统

Legal Events

Date Code Title Description
AS Assignment

Owner name: SIEMENS AKTIENGESELLSCHAFT, GERMANY

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:GETZE, DAVID;REEL/FRAME:026995/0379

Effective date: 20110916

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION