MX2012003246A - Configuraciones de alta remocion de co2 de alta presion y metodos. - Google Patents

Configuraciones de alta remocion de co2 de alta presion y metodos.

Info

Publication number
MX2012003246A
MX2012003246A MX2012003246A MX2012003246A MX2012003246A MX 2012003246 A MX2012003246 A MX 2012003246A MX 2012003246 A MX2012003246 A MX 2012003246A MX 2012003246 A MX2012003246 A MX 2012003246A MX 2012003246 A MX2012003246 A MX 2012003246A
Authority
MX
Mexico
Prior art keywords
solvent
rich solvent
semi
feed gas
absorber
Prior art date
Application number
MX2012003246A
Other languages
English (en)
Inventor
John Mark
Original Assignee
Fluor Tech Corp
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 Fluor Tech Corp filed Critical Fluor Tech Corp
Publication of MX2012003246A publication Critical patent/MX2012003246A/es

Links

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
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1456—Removing acid components
    • B01D53/1475—Removing carbon dioxide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1425—Regeneration of liquid absorbents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2256/00—Main component in the product gas stream after treatment
    • B01D2256/24—Hydrocarbons
    • B01D2256/245—Methane
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Gas Separation By Absorption (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

La presente invención se refiere a CO2 removido de gas de alimentación de alta presión en configuraciones y métodos de conformidad con la materia objeto poniendo en contacto el gas de alimentación con solvente semi-rico enfriado para formar una mezcla de dos fases que es vaporizada instantáneamente en la sección inferior de un absorbedor. El solvente rico del absorbedor es entonces reducido en presión para generar refrigeración para el solvente semi-rico y solvente pobre contactando de manera contracorriente el gas de alimentación parcialmente tratado en el absorbedor para producir el solvente semi-rico. Entre otras ventajas, el enfriamiento del gas de alimentación y solvente semi-rico por el solvente rico de presión reducida calienta el solvente rico para permitir regeneración mejorada del solvente, y la refrigeración externa y calentamiento del solvente pueden ser completamente evitados.
MX2012003246A 2009-09-18 2010-09-16 Configuraciones de alta remocion de co2 de alta presion y metodos. MX2012003246A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US24396909P 2009-09-18 2009-09-18
PCT/US2010/049058 WO2011034993A1 (en) 2009-09-18 2010-09-16 High pressure high co2 removal configurations and methods

Publications (1)

Publication Number Publication Date
MX2012003246A true MX2012003246A (es) 2012-04-10

Family

ID=43759003

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2012003246A MX2012003246A (es) 2009-09-18 2010-09-16 Configuraciones de alta remocion de co2 de alta presion y metodos.

Country Status (11)

Country Link
US (1) US9248398B2 (es)
EP (1) EP2477724A4 (es)
JP (1) JP2013505123A (es)
CN (1) CN102740951B (es)
AU (1) AU2010295593B2 (es)
CA (1) CA2774493C (es)
EA (1) EA201270439A1 (es)
IN (1) IN2012DN02348A (es)
MX (1) MX2012003246A (es)
WO (1) WO2011034993A1 (es)
ZA (1) ZA201202660B (es)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2536481A4 (en) 2010-02-17 2014-02-19 Fluor Tech Corp CONFIGURATIONS AND METHODS FOR REMOVAL OF HIGH PRESSURE ACID GAS IN THE PRODUCTION OF LOW SOFT SULFUR GAS
US10451344B2 (en) 2010-12-23 2019-10-22 Fluor Technologies Corporation Ethane recovery and ethane rejection methods and configurations
US20130202517A1 (en) * 2012-02-06 2013-08-08 General Electric Company Systems And Methods For Capturing Carbon Dioxide
WO2014066539A1 (en) 2012-10-24 2014-05-01 Fluor Technologies Corporation Integration methods of gas processing plant and nitrogen rejection unit for high nitrogen feed gases
DE102012021478A1 (de) * 2012-11-05 2014-05-08 Thyssenkrupp Uhde Gmbh Verfahren und Vorrichtung zur Entfernung von absorbierbaren Gasen aus unter Druck befindlichen, mit absorbierbaren Gasen verunreinigten Industriegasen ohne Zuführung von Kühlenergie
US10000713B2 (en) 2013-12-12 2018-06-19 Fluor Technologies Corporation Configurations and methods of flexible CO2 removal
US9901846B2 (en) 2014-11-21 2018-02-27 Gas Technology Institute Energy efficient solvent regeneration process for carbon dioxide capture
CA2976071C (en) 2015-02-09 2020-10-27 Fluor Technologies Corporation Methods and configuration of an ngl recovery process for low pressure rich feed gas
WO2017074323A1 (en) 2015-10-27 2017-05-04 Fluor Technologies Corporation Configurations and methods for processing high pressure acid gases with zero emissions
US10006701B2 (en) 2016-01-05 2018-06-26 Fluor Technologies Corporation Ethane recovery or ethane rejection operation
US10330382B2 (en) 2016-05-18 2019-06-25 Fluor Technologies Corporation Systems and methods for LNG production with propane and ethane recovery
US11725879B2 (en) 2016-09-09 2023-08-15 Fluor Technologies Corporation Methods and configuration for retrofitting NGL plant for high ethane recovery
CA3077409A1 (en) 2017-10-20 2019-04-25 Fluor Technologies Corporation Phase implementation of natural gas liquid recovery plants
CA3152981A1 (en) * 2019-10-01 2021-04-08 Michael J. Calderon Lean gas lng heavies removal process using ngl
US11484827B2 (en) * 2021-03-24 2022-11-01 Next Carbon Solutions, Llc Carbon dioxide sequestration in natural gas pipelines

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Publication number Priority date Publication date Assignee Title
US2826266A (en) * 1956-07-30 1958-03-11 Phillips Petroleum Co Removal of co2 from natural gas
US3664091A (en) 1969-06-27 1972-05-23 Fish Engineering & Constructio Process and system for removing acid gas from natural gas
US4833171A (en) * 1981-01-27 1989-05-23 Sweeney Maxwell P Synthesis gas system
AU562541B2 (en) 1981-01-27 1987-06-11 M.P. Sweeney Synthesis gas system
JPH0657287A (ja) 1992-08-07 1994-03-01 Maruha Corp 眼窩油類の安定化方法
AU4134796A (en) 1994-11-03 1996-05-31 Khanmamedov, Tufik K. Method and apparatus for removal of contaminates from refinery gas
JPH1150069A (ja) 1997-08-05 1999-02-23 Tosoh Corp 天然ガスの精製方法
WO2000030738A1 (en) 1998-11-23 2000-06-02 Fluor Corporation Split flow process and apparatus
US6235961B1 (en) * 1999-01-29 2001-05-22 Stone & Webster Engineering Corporation Process for pretreating cracked gas before caustic tower treatment in ehtylene plants
GB0015997D0 (en) * 2000-06-29 2000-08-23 Norske Stats Oljeselskap Method for mixing fluids
US7192468B2 (en) 2002-04-15 2007-03-20 Fluor Technologies Corporation Configurations and method for improved gas removal
CN1331563C (zh) 2002-09-17 2007-08-15 弗劳尔公司 除去酸性气体的设备和方法
CN100339150C (zh) * 2002-12-12 2007-09-26 弗劳尔公司 脱除酸性气体的装置和方法
JP4942935B2 (ja) 2002-12-17 2012-05-30 フルー・コーポレイシヨン ゼロに近い排出で酸性気体および汚染物質を除去する構成および方法
JP5036183B2 (ja) 2003-09-09 2012-09-26 フルオー・テクノロジーズ・コーポレイシヨン 改善された溶媒の使用および再生
JP5709153B2 (ja) * 2007-02-22 2015-04-30 フルオー・テクノロジーズ・コーポレイシヨン ガス化ストリームから二酸化炭素および水素を製造する構成および方法
CN102065976A (zh) 2008-06-26 2011-05-18 环球油品公司 用于冷却半贫物理溶剂的二氧化碳吸收器部分循环回流
CN102238994B (zh) 2008-10-02 2014-08-20 氟石科技公司 移除高压酸性气体的装置和方法

Also Published As

Publication number Publication date
WO2011034993A1 (en) 2011-03-24
AU2010295593A1 (en) 2012-04-12
IN2012DN02348A (es) 2015-08-21
CA2774493C (en) 2014-05-20
CN102740951A (zh) 2012-10-17
US9248398B2 (en) 2016-02-02
CN102740951B (zh) 2015-07-29
AU2010295593B2 (en) 2013-11-28
EP2477724A1 (en) 2012-07-25
ZA201202660B (en) 2014-10-29
EA201270439A1 (ru) 2012-09-28
EP2477724A4 (en) 2013-12-18
JP2013505123A (ja) 2013-02-14
CA2774493A1 (en) 2011-03-24
US20120227441A1 (en) 2012-09-13

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