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US20100212354A1 - Method of disposing of carbon dioxide - Google Patents

Method of disposing of carbon dioxide Download PDF

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Publication number
US20100212354A1
US20100212354A1 US12/666,664 US66666408A US2010212354A1 US 20100212354 A1 US20100212354 A1 US 20100212354A1 US 66666408 A US66666408 A US 66666408A US 2010212354 A1 US2010212354 A1 US 2010212354A1
Authority
US
United States
Prior art keywords
carbon dioxide
containing fraction
liquefaction
disposing
fractionation
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
US12/666,664
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English (en)
Inventor
Heinz Bauer
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.)
Linde GmbH
Original Assignee
Linde GmbH
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 Linde GmbH filed Critical Linde GmbH
Assigned to LINDE AKTIENGESELLSCHAFT reassignment LINDE AKTIENGESELLSCHAFT ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: BAUER, HEINZ
Publication of US20100212354A1 publication Critical patent/US20100212354A1/en
Abandoned legal-status Critical Current

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Classifications

    • 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
    • F25J3/0238—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 CnHm with 2 carbon atoms or more
    • 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
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0022—Hydrocarbons, e.g. natural gas
    • 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
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
    • F25J1/0032—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using the feed stream itself or separated fractions from it, i.e. "internal refrigeration"
    • F25J1/0045—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using the feed stream itself or separated fractions from it, i.e. "internal refrigeration" by vaporising a liquid return 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
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
    • F25J1/0047—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle
    • F25J1/0052—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant 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
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/006—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the refrigerant fluid used
    • F25J1/0095—Oxides of carbon, e.g. CO2
    • 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
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0244—Operation; Control and regulation; Instrumentation
    • F25J1/0245—Different modes, i.e. 'runs', of operation; Process control
    • F25J1/0249—Controlling refrigerant inventory, i.e. composition or quantity
    • F25J1/025—Details related to the refrigerant production or treatment, e.g. make-up supply from feed gas itself
    • 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
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
    • F25J1/0275—Construction and layout of liquefaction equipments, e.g. valves, machines adapted for special use of the liquefaction unit, e.g. portable or transportable devices
    • F25J1/0277—Offshore use, e.g. during shipping
    • F25J1/0278—Unit being stationary, e.g. on floating barge or fixed platform
    • 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
    • F25J3/0204—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 feed stream
    • F25J3/0209—Natural gas or substitute natural gas
    • 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
    • F25J3/0233—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 CnHm with 1 carbon atom or more
    • 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
    • F25J2220/00—Processes or apparatus involving steps for the removal of impurities
    • F25J2220/60—Separating impurities from natural gas, e.g. mercury, cyclic hydrocarbons
    • F25J2220/66—Separating acid gases, e.g. CO2, SO2, H2S or RSH
    • 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.

Definitions

  • the invention relates to a method and also an arrangement for disposing of one of more carbon dioxide-containing fractions which occur at one or more sites of a fractionation and/or liquefaction process such as, for example, a natural gas liquefaction process.
  • carbon dioxide sources are, for example, the residual gas originating from acid gas removal or amine scrubbing and also the exhaust gas streams of gas turbines and steam generators.
  • the abovementioned carbon dioxide-containing fractions have been to date released essentially untreated to the atmosphere. The reason for this is to be seen in the fact that although limiting values are prescribed for hydrocarbons and sulphur compounds by the German TA Lucas [German Instructions on Air Pollution], they are not for carbon dioxide; emission thereof is therefore still permitted without restrictions. In view of current discussions with respect to the carbon dioxide problem, such a procedure can now be considered outmoded.
  • carbon dioxide is used as refrigerant.
  • pure carbon dioxide refrigerant cycles are suitable for precooling the natural gas to be liquefied; such a natural gas liquefaction method is disclosed, for example, in U.S. Pat. No. 6,722,157. Provision and, in particular, disposal of the carbon dioxide necessary for these (precooling) refrigerant cycles, however, have not to date been given sufficient attention.
  • a method of disposing of one or more carbon dioxide-containing fractions which is characterized in that the carbon dioxide-containing fraction(s) is or are subjected to a purification and/or liquefaction and subsequently sequestered.
  • the arrangement of the invention for disposing of one or more carbon dioxide-containing fractions is characterized by at least one purification unit and/or at least one liquefaction unit to which is or are fed the carbon dioxide-containing fraction(s), and also by means for feeding the purified and/or liquefied carbon dioxide-containing fraction(s) to a sequestration.
  • the black boxes A, A′ and A′′ shown in the FIGURE represent a plurality of “carbon dioxide sources” such as, for example, one or more amine scrubbers (A), one or more gas turbines (A′) and also one or more steam generators (A′′), as are generally provided in the context of fractionation and/or liquefaction processes.
  • carbon dioxide sources such as, for example, one or more amine scrubbers (A), one or more gas turbines (A′) and also one or more steam generators (A′′), as are generally provided in the context of fractionation and/or liquefaction processes.
  • the carbon dioxide-containing gas or exhaust gas occurring in these “carbon dioxide sources” is taken off for lines 1 , 2 and 3 , combined and fed via a shared line 4 to a purification unit B.
  • This purification unit B is preferably constructed as a purification unit operating by absorption, adsorption and/or permeation.
  • the purification unit B comprises, where this is necessary in individual cases, a drying unit for the carbon dioxide-containing fraction which is fed.
  • the carbon dioxide-containing fraction taken off from the purification unit B via line 5 preferably has a carbon dioxide content of greater than 90% by volume.
  • This fraction is then compressed to the extent that, in the downstream liquefaction unit C, liquefaction of the carbon dioxide-containing fraction can proceed against a suitable medium, such as, for example, cooling water, air or another suitable fluid.
  • a suitable medium such as, for example, cooling water, air or another suitable fluid.
  • the liquefied carbon dioxide-containing fraction can then according to the invention be used in whole or at least in part as refrigerant, for example for precooling in the context of a natural gas liquefaction process, or for cooling in the removal of lighter hydrocarbons, such as C 2+ or C 3+ hydrocarbons, from natural gas.
  • This (pre)cooling is intended to be shown by black box D to which the carbon dioxide-containing fraction is fed via line 6 .
  • the carbon dioxide-containing fraction used as refrigerant (black box D) and “exhausted” is fed via line 7 back to the liquefaction unit C and in this is optionally reliquefied.
  • the fraction of liquefied carbon dioxide-containing fraction which is intended to be fed to a sequestration is pumped to the desired sequestration pressure by means of a single-stage or multistage pump unit 9 .
  • This sequestration pressure is preferably above 100 bar.
  • the carbon dioxide-containing fraction is fed via line 8 to a suitable sequestration E such as, for example, a subterraneous store or cavern.
  • the method according to the invention and also the arrangement according to the invention for disposing of one or more carbon dioxide-containing fractions is suitable, in particular, for floating natural gas production plants since, in these, owing to the safety risks associated with certain hydrocarbon mixtures, carbon dioxide is preferred as refrigerant for the precooling.
  • the invention is always used when, firstly, within the fractionation process and/or liquefaction process, a plurality of carbon dioxide-containing fractions occur, and secondly, liquid carbon dioxide or a liquefied carbon dioxide-containing fraction is desired or necessary as refrigerant.

Landscapes

  • Engineering & Computer Science (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Ocean & Marine Engineering (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)
US12/666,664 2007-06-26 2008-06-05 Method of disposing of carbon dioxide Abandoned US20100212354A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE102007029434.6 2007-06-26
DE102007029434A DE102007029434A1 (de) 2007-06-26 2007-06-26 Verfahren zur Entsorgung von Kohlendioxid
PCT/EP2008/004505 WO2009000393A2 (de) 2007-06-26 2008-06-05 Verfahren zur entsorgung von kohlendioxid

Publications (1)

Publication Number Publication Date
US20100212354A1 true US20100212354A1 (en) 2010-08-26

Family

ID=40075875

Family Applications (1)

Application Number Title Priority Date Filing Date
US12/666,664 Abandoned US20100212354A1 (en) 2007-06-26 2008-06-05 Method of disposing of carbon dioxide

Country Status (9)

Country Link
US (1) US20100212354A1 (es)
CN (1) CN101874187A (es)
AU (1) AU2008267511A1 (es)
DE (1) DE102007029434A1 (es)
MX (1) MX2009013404A (es)
MY (1) MY177037A (es)
NO (1) NO20100108L (es)
RU (1) RU2482407C2 (es)
WO (1) WO2009000393A2 (es)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120174621A1 (en) * 2011-01-06 2012-07-12 General Electric Company Carbon dioxide liquefaction system
DE102013011640A1 (de) * 2013-07-11 2015-01-29 Linde Aktiengesellschaft Verfahren zum Abtrennen von Sauergasen aus Erdgas

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3962881A (en) * 1974-02-19 1976-06-15 Airco, Inc. Liquefaction of a vapor utilizing refrigeration of LNG
US20020144506A1 (en) * 1995-06-07 2002-10-10 Fermin Viteri Hydrocarbon combustion power generation system with CO2 sequestration
US20080307966A1 (en) * 2007-02-12 2008-12-18 Donald Leo Stinson System for Separating Carbon Dioxide from a Produced Gas with a Methanol Removal System
US20100006803A1 (en) * 2008-07-10 2010-01-14 Jose Luis Bravo Method of treating a high-pressure hydrocarbon stream having a high carbon dioxide content to yield a high purity hydrocarbon gas stream and a sequestration ready carbon dioxide gas stream

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JPS5973416A (ja) * 1982-10-15 1984-04-25 Ishikawajima Harima Heavy Ind Co Ltd 液化天然ガスの燃焼排ガスからの液化炭酸製造方法
SU1366821A1 (ru) * 1984-06-28 1988-01-15 Специализированное Управление "Узоргэнергогаз" Способ очистки природного газа от кислых компонентов
CN1035478A (zh) * 1989-03-16 1989-09-13 于洪喜 二氧化碳生产工艺
JPH0663699B2 (ja) * 1990-06-14 1994-08-22 財団法人電力中央研究所 液化天然ガス焚き火力発電所から排出される二酸化炭素の回収方法
US5681360A (en) * 1995-01-11 1997-10-28 Acrion Technologies, Inc. Landfill gas recovery
US6070431A (en) * 1999-02-02 2000-06-06 Praxair Technology, Inc. Distillation system for producing carbon dioxide
JP4138399B2 (ja) * 2002-08-21 2008-08-27 三菱重工業株式会社 液化天然ガスの製造方法
CN2606739Y (zh) * 2003-03-14 2004-03-17 大连理工大学 吸附精馏提纯二氧化碳装置
US6722157B1 (en) 2003-03-20 2004-04-20 Conocophillips Company Non-volatile natural gas liquefaction system
US7076969B2 (en) * 2004-01-19 2006-07-18 Air Products And Chemicals, Inc. System for supply and delivery of high purity and ultrahigh purity carbon dioxide

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3962881A (en) * 1974-02-19 1976-06-15 Airco, Inc. Liquefaction of a vapor utilizing refrigeration of LNG
US20020144506A1 (en) * 1995-06-07 2002-10-10 Fermin Viteri Hydrocarbon combustion power generation system with CO2 sequestration
US20080307966A1 (en) * 2007-02-12 2008-12-18 Donald Leo Stinson System for Separating Carbon Dioxide from a Produced Gas with a Methanol Removal System
US20100006803A1 (en) * 2008-07-10 2010-01-14 Jose Luis Bravo Method of treating a high-pressure hydrocarbon stream having a high carbon dioxide content to yield a high purity hydrocarbon gas stream and a sequestration ready carbon dioxide gas stream

Also Published As

Publication number Publication date
RU2010102252A (ru) 2011-08-10
WO2009000393A3 (de) 2014-02-20
NO20100108L (no) 2010-01-22
RU2482407C2 (ru) 2013-05-20
CN101874187A (zh) 2010-10-27
WO2009000393A2 (de) 2008-12-31
AU2008267511A1 (en) 2008-12-31
MY177037A (en) 2020-09-02
DE102007029434A1 (de) 2009-01-02
MX2009013404A (es) 2010-01-25

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AS Assignment

Owner name: LINDE AKTIENGESELLSCHAFT, GERMANY

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:BAUER, HEINZ;REEL/FRAME:024335/0355

Effective date: 20100427

STCB Information on status: application discontinuation

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