ATE520761T1 - Verfahren und system zur entfernung von h2s aus einem erdgasstrom - Google Patents

Verfahren und system zur entfernung von h2s aus einem erdgasstrom

Info

Publication number
ATE520761T1
ATE520761T1 AT08766847T AT08766847T ATE520761T1 AT E520761 T1 ATE520761 T1 AT E520761T1 AT 08766847 T AT08766847 T AT 08766847T AT 08766847 T AT08766847 T AT 08766847T AT E520761 T1 ATE520761 T1 AT E520761T1
Authority
AT
Austria
Prior art keywords
removal
natural gas
gas stream
stream
natural
Prior art date
Application number
AT08766847T
Other languages
English (en)
Inventor
Marco Betting
Willink Cornelis Antonie Tjeenk
Bakel Robert Petrus Van
Original Assignee
Twister Bv
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 Twister Bv filed Critical Twister Bv
Application granted granted Critical
Publication of ATE520761T1 publication Critical patent/ATE520761T1/de

Links

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
    • F25J3/0204—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
    • 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
    • B01D53/24—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 centrifugal force
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/48—Sulfur compounds
    • B01D53/52—Hydrogen sulfide
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10—Working-up natural gas or synthetic natural gas
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10—Working-up natural gas or synthetic natural gas
    • C10L3/101—Removal of contaminants
    • C10L3/102—Removal of contaminants of acid contaminants
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10—Working-up natural gas or synthetic natural gas
    • C10L3/101—Removal of contaminants
    • C10L3/102—Removal of contaminants of acid contaminants
    • C10L3/103—Sulfur containing contaminants
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/30—Sulfur compounds
    • B01D2257/304—Hydrogen sulfide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/06—Polluted 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
    • F25J2200/00—Processes or apparatus using separation by rectification
    • F25J2200/70—Refluxing the column with a condensed part of the feed stream, i.e. fractionator top is stripped or self-rectified
    • 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
    • F25J2205/00—Processes or apparatus using other separation and/or other processing means
    • F25J2205/10—Processes or apparatus using other separation and/or other processing means using combined expansion and separation, e.g. in a vortex tube, "Ranque tube" or a "cyclonic fluid separator", i.e. combination of an isentropic nozzle and a cyclonic separator; Centrifugal separation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Separating Particles In Gases By Inertia (AREA)
  • Cyclones (AREA)
AT08766847T 2007-06-27 2008-06-27 Verfahren und system zur entfernung von h2s aus einem erdgasstrom ATE520761T1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP07111145 2007-06-27
PCT/NL2008/050424 WO2009002174A2 (en) 2007-06-27 2008-06-27 Method and system for removing hydrogen sulphide (h2s) from a natural gas stream

Publications (1)

Publication Number Publication Date
ATE520761T1 true ATE520761T1 (de) 2011-09-15

Family

ID=39302104

Family Applications (1)

Application Number Title Priority Date Filing Date
AT08766847T ATE520761T1 (de) 2007-06-27 2008-06-27 Verfahren und system zur entfernung von h2s aus einem erdgasstrom

Country Status (13)

Country Link
US (1) US9500404B2 (de)
EP (1) EP2160452B1 (de)
CN (1) CN101778931B (de)
AR (1) AR067341A1 (de)
AT (1) ATE520761T1 (de)
CA (1) CA2691743C (de)
EA (1) EA015953B1 (de)
EG (1) EG26358A (de)
MY (1) MY147349A (de)
PE (1) PE20090523A1 (de)
RU (1) RU2462295C2 (de)
TW (1) TW200912228A (de)
WO (1) WO2009002174A2 (de)

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NL2002691C2 (en) * 2009-03-31 2010-10-04 Romico Hold A V V Method for separating a medium mixture into fractions.
CA2758050C (en) * 2009-04-07 2017-11-21 Twister B.V. Separation system comprising a swirl valve
EP2365852B1 (de) * 2009-07-13 2022-04-20 Dexpro Corporation Verfahren zur entfernung kondensierbarer bestandteile aus einer flüssigkeit
DE102009037460A1 (de) * 2009-08-13 2011-02-17 Siemens Aktiengesellschaft Abscheiden von Schwefelwasserstoff
US8858680B2 (en) 2010-06-01 2014-10-14 Shell Oil Company Separation of oxygen containing gases
US8663369B2 (en) 2010-06-01 2014-03-04 Shell Oil Company Separation of gases produced by combustion
US8858679B2 (en) 2010-06-01 2014-10-14 Shell Oil Company Separation of industrial gases
WO2011153151A1 (en) 2010-06-01 2011-12-08 Shell Oil Company Low emission power plant
MY164712A (en) * 2010-09-03 2018-01-30 Twister Bv Refining system and method for refining a feed gas stream
SG10201508651UA (en) * 2010-10-20 2015-11-27 Kirtikumar Natubhai Patel Process for separating and recovering ethane and heavier hydrocarbons from lng
CN103084285B (zh) * 2011-11-03 2015-06-17 西安长庆科技工程有限责任公司 一种天然气的气液分离装置及方法
CA2763081C (en) * 2011-12-20 2019-08-13 Jose Lourenco Method to produce liquefied natural gas (lng) at midstream natural gas liquids (ngls) recovery plants.
RU2493501C1 (ru) * 2012-03-02 2013-09-20 Олег Савельевич Кочетов Приточно-вытяжная установка с утилизацией тепла
CA2790961C (en) 2012-05-11 2019-09-03 Jose Lourenco A method to recover lpg and condensates from refineries fuel gas streams.
CA2798057C (en) 2012-12-04 2019-11-26 1304342 Alberta Ltd. A method to produce lng at gas pressure letdown stations in natural gas transmission pipeline systems
CN103111173B (zh) * 2013-01-21 2015-09-02 江汉大学 一种烟气净化系统及其方法
CA2813260C (en) 2013-04-15 2021-07-06 Mackenzie Millar A method to produce lng
AR096132A1 (es) 2013-05-09 2015-12-09 Exxonmobil Upstream Res Co Separar dióxido de carbono y sulfuro de hidrógeno de un flujo de gas natural con sistemas de co-corriente en contacto
AU2015225689B2 (en) * 2014-03-07 2019-01-03 Conocophillips Company Heat exchanger system with mono-cyclone inline separator
US10288347B2 (en) 2014-08-15 2019-05-14 1304338 Alberta Ltd. Method of removing carbon dioxide during liquid natural gas production from natural gas at gas pressure letdown stations
MX2017007708A (es) 2015-01-09 2017-10-27 Exxonmobil Upstream Res Co Separando impurezas de una corriente de fluido usando contactores multiples de corrientes en igual sentido.
SG11201705110QA (en) 2015-02-17 2017-09-28 Exxonmobil Upstream Res Co Inner surface features for co-current contactors
MX2017011064A (es) 2015-03-13 2017-11-10 Exxonmobil Upstream Res Co Dispositivo de coalescencia para contactores de co-corriente.
CA2997628C (en) 2015-09-16 2022-10-25 1304342 Alberta Ltd. A method of preparing natural gas at a gas pressure reduction stations to produce liquid natural gas (lng)
ES2755416T3 (es) * 2015-12-03 2020-04-22 Shell Int Research Método de licuefacción de una corriente de gas contaminado que contiene hidrocarburos con CO2
KR101784996B1 (ko) 2016-02-02 2017-11-06 한국기계연구원 황화수소 제거 장치
US11000795B2 (en) 2017-06-15 2021-05-11 Exxonmobil Upstream Research Company Fractionation system using compact co-current contacting systems
WO2018231332A1 (en) 2017-06-15 2018-12-20 Exxonmobil Upstream Research Company Fractionation system using bundler compact co-current contacting systems
MX394342B (es) 2017-06-20 2025-03-24 Exxonmobil Upstream Res Co Sistemas de contacto compactos y metodos para depurar compuestos que contienen azufre.
MY202923A (en) 2017-08-21 2024-05-29 Exxonmobil Upstream Res Co Integration of cold solvent and acid gas removal
CN112263894B (zh) * 2020-11-26 2025-03-18 西南石油大学 一种针对含硫气体的离子液体脱硫方法及设备
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Also Published As

Publication number Publication date
PE20090523A1 (es) 2009-05-24
EA015953B1 (ru) 2011-12-30
TW200912228A (en) 2009-03-16
EG26358A (en) 2013-08-26
CA2691743A1 (en) 2008-12-31
EP2160452A2 (de) 2010-03-10
CA2691743C (en) 2017-06-20
EA201000072A1 (ru) 2010-08-30
CN101778931A (zh) 2010-07-14
WO2009002174A3 (en) 2009-02-19
US20110036122A1 (en) 2011-02-17
WO2009002174A2 (en) 2008-12-31
RU2010102536A (ru) 2011-08-10
EP2160452B1 (de) 2011-08-17
CN101778931B (zh) 2013-03-27
US9500404B2 (en) 2016-11-22
AR067341A1 (es) 2009-10-07
MY147349A (en) 2012-11-30
RU2462295C2 (ru) 2012-09-27

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