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PE20090523A1 - Metodo y sistema para remover h2s de una corriente de gas natural - Google Patents

Metodo y sistema para remover h2s de una corriente de gas natural

Info

Publication number
PE20090523A1
PE20090523A1 PE2008001108A PE2008001108A PE20090523A1 PE 20090523 A1 PE20090523 A1 PE 20090523A1 PE 2008001108 A PE2008001108 A PE 2008001108A PE 2008001108 A PE2008001108 A PE 2008001108A PE 20090523 A1 PE20090523 A1 PE 20090523A1
Authority
PE
Peru
Prior art keywords
fraction
natural gas
hydrogen sulfide
refrigerated
current
Prior art date
Application number
PE2008001108A
Other languages
English (en)
Inventor
Marco Betting
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
Publication of PE20090523A1 publication Critical patent/PE20090523A1/es

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)
  • General Engineering & Computer Science (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (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)

Abstract

SE REFIERE A UN METODO QUE COMPRENDE METANO Y SULFURO DE HIDROGENO, E INCLUYE: A) REFRIGERAR EL GAS NATURAL EN UN MONTAJE INTERCAMBIADOR DE CALOR; B) ALIMENTAR POR LO MENOS PARTE DE LA CORRIENTE DE GAS NATURAL REFIRGERADO A TRAVES DE UN CONDUCTO DE ALIMENTACION EN UN DISPOSITIVO CICLONICO DE EXPANSION Y SEPARACION EN EL CUAL LA CORRIENTE DE GAS NATURAL REFRIGERADO SE EXPANDE EN UNA BOQUILLA Y DE ESTE MODO REFRIGERAR LUEGO A UNA TEMPERATURA Y PRESION DEBAJO DEL PUNTO DE ROCIO DEL SULFURO DE HIDROGENO Y SEPARAR INDUCIENDO LA CORRIENTE DE GAS NATURAL REFRIGERADO A REMOLINO EN UNA CAMARA TUBULAR DE SEPARACION; C) ALIMENTAR LA FRACCION DE FLUIDO REFRIGERADO DE BAJA DENSIDAD A UN CONDUCTO DE GAS DE PRODUCTO QUE SE CONECTA CON UN INTERCAMBIADOR DE CALOR PARA REFRIGERAR LA CORRIENTE DE GAS NATURAL ALIMENTADA AL DISPOSITIVO CICLONICO DE EXPANSION Y SEPARACION; Y D) ALIMENTAR LA FRACCION DE FLUIDO REFRIGERADO DE ALTA DENSIDAD A UNA COLUMNA DE FRACCIONAMIENTO PARA UNA SEPARACION ADICIONAL, Y EN DONDE LA COLUMNA DE FRACCIONAMIENTO ESTA CONFIGURADA PARA SEPARAR LA FRACCION DE FLUIDO DE ALTA DENSIDAD DESCARGADA POR EL DISPOSITIVO CICLONICO DE EXPANSION Y SEPARACION EN UNA FRACCION DE FONDO ENRIQUECIDA CON SULFURO DE HIDROGENO Y AGOTADA DE METANO Y UNA FRACCION SUPERIOR AGOTADA DE SULFURO DE HIDROGENO Y ENRIQUECIDA CON METANO
PE2008001108A 2007-06-27 2008-06-27 Metodo y sistema para remover h2s de una corriente de gas natural PE20090523A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP07111145 2007-06-27

Publications (1)

Publication Number Publication Date
PE20090523A1 true PE20090523A1 (es) 2009-05-24

Family

ID=39302104

Family Applications (1)

Application Number Title Priority Date Filing Date
PE2008001108A PE20090523A1 (es) 2007-06-27 2008-06-27 Metodo y sistema para remover h2s de una corriente de gas natural

Country Status (13)

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

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AU2010273123A1 (en) 2009-07-13 2011-01-20 James Maddocks Process for removing condensable components from a fluid
DE102009037460A1 (de) * 2009-08-13 2011-02-17 Siemens Aktiengesellschaft Abscheiden von Schwefelwasserstoff
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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
AU2011296633B2 (en) 2010-09-03 2016-07-14 Twister B.V. Refining system and method for refining a feed gas stream
MX2013004441A (es) * 2010-10-20 2014-07-24 Rohit N Patel Proceso para la separacion y recuperacion de etanol y los hidrocarburos mas pesados de gas natural liquido.
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 Mackenzie Millar 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
EP3114422B1 (en) * 2014-03-07 2018-04-11 Conoco Phillips 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
MY182017A (en) 2015-01-09 2021-01-18 Exxonmobil Upstream Res Co Separating impurities from a fluid stream using multiple co-current contactors
KR101964584B1 (ko) 2015-02-17 2019-04-03 엑손모빌 업스트림 리서치 캄파니 병류 컨택터에 대한 내부 표면 특징
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AU2016363562B2 (en) * 2015-12-03 2019-06-20 Shell Internationale Research Maatschappij B.V. Method of liquefying a CO2 contaminated hydrocarbon-containing gas stream
KR101784996B1 (ko) 2016-02-02 2017-11-06 한국기계연구원 황화수소 제거 장치
WO2018231347A1 (en) 2017-06-15 2018-12-20 Exxonmobil Upstream Research Company Fractionation system using compact co-current contacting systems
AU2018283902B9 (en) 2017-06-15 2021-08-05 Exxonmobil Upstream Research Company Fractionation system using bundler compact co-current contacting systems
CN110769917B (zh) 2017-06-20 2022-06-07 埃克森美孚上游研究公司 用于清除含硫化合物的紧凑的接触系统和方法
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
AR067341A1 (es) 2009-10-07
ATE520761T1 (de) 2011-09-15
CA2691743A1 (en) 2008-12-31
CN101778931A (zh) 2010-07-14
US9500404B2 (en) 2016-11-22
RU2010102536A (ru) 2011-08-10
EP2160452A2 (en) 2010-03-10
US20110036122A1 (en) 2011-02-17
MY147349A (en) 2012-11-30
WO2009002174A3 (en) 2009-02-19
CA2691743C (en) 2017-06-20
EA201000072A1 (ru) 2010-08-30
EG26358A (en) 2013-08-26
EP2160452B1 (en) 2011-08-17
WO2009002174A2 (en) 2008-12-31
TW200912228A (en) 2009-03-16
CN101778931B (zh) 2013-03-27
EA015953B1 (ru) 2011-12-30
RU2462295C2 (ru) 2012-09-27

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