[go: up one dir, main page]

EA200800827A1 - Способ и устройство для удаления кислых веществ из потока природного газа - Google Patents

Способ и устройство для удаления кислых веществ из потока природного газа

Info

Publication number
EA200800827A1
EA200800827A1 EA200800827A EA200800827A EA200800827A1 EA 200800827 A1 EA200800827 A1 EA 200800827A1 EA 200800827 A EA200800827 A EA 200800827A EA 200800827 A EA200800827 A EA 200800827A EA 200800827 A1 EA200800827 A1 EA 200800827A1
Authority
EA
Eurasian Patent Office
Prior art keywords
zone
natural gas
gas
formation
acidic substances
Prior art date
Application number
EA200800827A
Other languages
English (en)
Other versions
EA012227B1 (ru
Inventor
Аллан Харт
Роберт Амин
Original Assignee
Кул Энерджи Лимитед
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=37864568&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EA200800827(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Priority claimed from AU2005905089A external-priority patent/AU2005905089A0/en
Application filed by Кул Энерджи Лимитед filed Critical Кул Энерджи Лимитед
Publication of EA200800827A1 publication Critical patent/EA200800827A1/ru
Publication of EA012227B1 publication Critical patent/EA012227B1/ru

Links

Classifications

    • 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
    • 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
    • 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
    • B01D53/1462—Removing mixtures of hydrogen sulfide and 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
    • B01D53/1493—Selection of liquid materials for use as absorbents
    • 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
    • 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
    • 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
    • F25J3/0242—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 3 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
    • 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
    • B01D2257/30—Sulfur compounds
    • B01D2257/306—Organic sulfur compounds, e.g. mercaptans
    • 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
    • B01D2257/308—Carbonoxysulfide COS
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/60—Heavy metals or heavy metal compounds
    • B01D2257/602—Mercury or mercury compounds
    • 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
    • F25J2200/02—Processes or apparatus using separation by rectification in a single pressure main column system
    • 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
    • F25J2200/90—Details relating to column internals, e.g. structured packing, gas or liquid distribution
    • 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
    • F25J2205/02—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
    • F25J2205/04—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum in the feed line, i.e. upstream of the fractionation step
    • 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
    • F25J2205/20—Processes or apparatus using other separation and/or other processing means using solidification of components
    • 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
    • F25J2205/50—Processes or apparatus using other separation and/or other processing means using absorption, i.e. with selective solvents or lean oil, heavier CnHm and including generally a regeneration step for the solvent or lean oil
    • 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
    • F25J2240/00—Processes or apparatus involving steps for expanding of process streams
    • F25J2240/02—Expansion of a process fluid in a work-extracting turbine (i.e. isentropic expansion), e.g. 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
    • F25J2240/00—Processes or apparatus involving steps for expanding of process streams
    • F25J2240/40—Expansion without extracting work, i.e. isenthalpic throttling, e.g. JT valve, regulating valve or venturi, or isentropic nozzle, e.g. Laval
    • 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
    • F25J2270/00—Refrigeration techniques used
    • F25J2270/12—External refrigeration with liquid vaporising loop
    • 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
    • F25J2270/00—Refrigeration techniques used
    • F25J2270/60—Closed external refrigeration cycle with single component refrigerant [SCR], e.g. C1-, C2- or C3-hydrocarbons
    • 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
    • F25J2270/00—Refrigeration techniques used
    • F25J2270/66—Closed external refrigeration cycle with multi component refrigerant [MCR], e.g. mixture of hydrocarbons
    • 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
    • F25J2290/40—Vertical layout or arrangement of cold equipments within in the cold box, e.g. columns, condensers, heat exchangers etc.
    • 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

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Gas Separation By Absorption (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

Предлагается способ удаления кислых веществ из подаваемого потока дегидратированного природного газа. Подаваемый поток дегидратированного природного газа охлаждается до условий, при которых образуется суспензия твердых кислых веществ и углеводородных жидкостей совместно с газовым потоком, содержащим газообразные кислые вещества. Газовый поток, содержащий газообразные кислые вещества, затем отделяется от суспензии и обрабатывается жидким растворителем и тем самым образуется жидкий раствор кислых веществ и продукт в виде потока дегидратированного раскисленного природного газа. Также предлагается устройство для удаления кислых веществ из подаваемого потока дегидратированного природного газа. Устройство имеет емкость с зоной образования твердых веществ, связанной потоками с зоной газовой сольватации. Зона образования твердых веществ сконфигурирована для облегчения образования суспензии из твердых кислых веществ и углеводородных жидкостей, и газового потока, содержащего газообразные кислые вещества. Зона газовой сольватации сконфигурирована для облегчения образования жидкого раствора кислых веществ. Устройство имеет вход для ввода подаваемого потока дегидратированного природного газа в зону образования твердых веществ, трубопровод, сконфигурированный для направления газового потока из зоны образования твердых веществ в зону газовой сольватации, и вход для ввода жидкого растворителя в зону газовой сольватации.
EA200800827A 2005-09-15 2006-09-15 Способ и устройство для удаления кислых веществ из потока природного газа EA012227B1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
AU2005905089A AU2005905089A0 (en) 2005-09-15 Process and apparatus for removal of sour species from a natural gas stream
PCT/AU2006/001356 WO2007030888A1 (en) 2005-09-15 2006-09-15 Process and apparatus for removal of sour species from a natural gas stream

Publications (2)

Publication Number Publication Date
EA200800827A1 true EA200800827A1 (ru) 2008-06-30
EA012227B1 EA012227B1 (ru) 2009-08-28

Family

ID=37864568

Family Applications (1)

Application Number Title Priority Date Filing Date
EA200800827A EA012227B1 (ru) 2005-09-15 2006-09-15 Способ и устройство для удаления кислых веществ из потока природного газа

Country Status (9)

Country Link
US (1) US20100147022A1 (ru)
EP (1) EP1931755A4 (ru)
CN (1) CN101283078A (ru)
AU (2) AU2006291954C1 (ru)
CA (1) CA2622570A1 (ru)
EA (1) EA012227B1 (ru)
MY (1) MY145090A (ru)
NZ (1) NZ566742A (ru)
WO (1) WO2007030888A1 (ru)

Families Citing this family (60)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2667429C (en) * 2006-10-24 2015-04-07 Shell Canada Limited Process for producing purified natural gas
CA2674618C (en) 2007-01-19 2015-02-10 Exxonmobil Upstream Research Company Integrated controlled freeze zone (cfz) tower and dividing wall (dwc) for enhanced hydrocarbon recovery
EP2118238A1 (en) * 2007-02-09 2009-11-18 Cool Energy Limited Process and apparatus for depleting carbon dioxide content in a natural gas feedstream containing ethane and c3+ hydrocarbons
GB0709433D0 (en) * 2007-05-16 2007-06-27 Gasconsult Ltd Process for removal of carbon dioxide from gases
WO2008152030A1 (en) * 2007-06-12 2008-12-18 Shell Internationale Research Maatschappij B.V. Process for the purification of methane containing streams by cooling and extraction
AU2009253116B2 (en) * 2008-05-30 2012-10-11 Shell Internationale Research Maatschappij B.V. Producing purified hydrocarbon gas from a gas stream comprising hydrocarbons and acidic contaminants
CA2726229A1 (en) * 2008-05-30 2009-12-03 Shell Internationale Research Maatschappij B.V. Process for producing purified hydrocarbon gas
CA2730637A1 (en) * 2008-07-10 2010-01-14 Shell Internationale Research Maatschappij B.V. Process for removing a gaseous contaminant from a contaminated gas stream
RU2011106108A (ru) * 2008-07-18 2012-08-27 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL) Двухстадийный способ производства очищенного газа
AU2009286701B2 (en) 2008-08-29 2012-09-13 Shell Internationale Research Maatschappij B.V. Process and apparatus for removing gaseous contaminants from gas stream comprising gaseous contaminants
RU2011133062A (ru) * 2009-01-08 2013-02-20 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Способ удаления газообразных примесей из потока газа, содержащего газообразные примеси, и устройство для его осуществления
US20120006055A1 (en) * 2009-01-08 2012-01-12 Helmar Van Santen Process and apparatus for separating a gaseous product from a feed stream comprising contaminants
CN102405275B (zh) 2009-04-20 2015-01-14 埃克森美孚上游研究公司 从烃气流中去除酸性气体的低温系统和去除酸性气体的方法
EP2255863A1 (en) * 2009-05-26 2010-12-01 Shell Internationale Research Maatschappij B.V. Process for removing gaseous contaminants from a liquid phase containing feed stream
EP2255864A1 (en) * 2009-05-26 2010-12-01 Shell Internationale Research Maatschappij B.V. Process for removing gaseous contaminants from a feed stream
WO2011026170A1 (en) * 2009-09-01 2011-03-10 Cool Energy Limited Process and apparatus for reducing the concentration of a sour species in a sour gas
JP5791609B2 (ja) * 2009-09-09 2015-10-07 エクソンモービル アップストリーム リサーチ カンパニー 炭化水素ガス流から酸性ガスを除去する極低温システム
CA2683983A1 (en) * 2009-10-21 2011-04-21 Carbon Solutions Inc. Stabilization and remote recovery of acid gas fractions from sour wellsite gas
MX338688B (es) 2010-01-22 2016-04-27 Exxonmobil Upstream Res Co Eliminacion de gases acidos de una corriente de gas, con captura y secuestro de co2.
SG10201500810PA (en) * 2010-02-03 2015-04-29 Exxonmobil Upstream Res Co Systems and methods for using cold liquid to remove solidifiable gas components from process gas streams
GB201004638D0 (en) 2010-03-19 2010-05-05 Univ Belfast Separation of gases
FR2959512B1 (fr) 2010-04-29 2012-06-29 Total Sa Procede de traitement d'un gaz naturel contenant du dioxyde de carbone
BR112013000263A2 (pt) 2010-07-30 2016-05-24 Exxonmobil Upstream Res Co sistemas criogênicos para remover gases ácidos de uma corrente de gás de hidrocarboneto usando dispostivos de separação em co-corrente
FR2964390B1 (fr) * 2010-09-03 2012-09-28 Total Sa Procede de traitement d'un gaz naturel contenant du dioxyde de carbone
CN103201013B (zh) * 2010-09-03 2017-02-22 缠绕机公司 用于精炼原料气流的精炼系统和方法
US8635885B2 (en) * 2010-10-15 2014-01-28 Fluor Technologies Corporation Configurations and methods of heating value control in LNG liquefaction plant
DE102011084733A1 (de) * 2011-10-18 2013-04-18 Victoria Capital Investments Group LTD. Verfahren und Vorrichtung zur Entwässerung eines C02-haltigen Gases
EP2785433A1 (en) * 2011-12-01 2014-10-08 Statoil Petroleum AS Process with continuously stirred tank reactor absorber and flash tank stripper
CA2867287C (en) 2012-03-21 2019-06-11 Exxonmobil Upstream Research Company Separating carbon dioxide and ethane from a mixed stream
WO2013144671A1 (en) * 2012-03-27 2013-10-03 Total Sa Cryogenic separation process of a feed gas stream containing carbon dioxide and methane
US20150093313A1 (en) * 2013-09-30 2015-04-02 Uop Llc Ionic liquid and solvent mixtures for hydrogen sulfide removal
WO2015084494A2 (en) 2013-12-06 2015-06-11 Exxonmobil Upstream Research Company Method and device for separating hydrocarbons and contaminants with a spray assembly
EA031531B1 (ru) 2013-12-06 2019-01-31 Эксонмобил Апстрим Рисерч Компани Способ и устройство для разделения углеводородов и загрязняющих примесей с помощью нагревательного устройства для дестабилизации и/или предотвращения адгезии твердых веществ
WO2015084495A2 (en) 2013-12-06 2015-06-11 Exxonmobil Upstream Research Company Method and system of maintaining a liquid level in a distillation tower
US9874395B2 (en) 2013-12-06 2018-01-23 Exxonmobil Upstream Research Company Method and system for preventing accumulation of solids in a distillation tower
US9803918B2 (en) 2013-12-06 2017-10-31 Exxonmobil Upstream Research Company Method and system of dehydrating a feed stream processed in a distillation tower
US9562719B2 (en) 2013-12-06 2017-02-07 Exxonmobil Upstream Research Company Method of removing solids by modifying a liquid level in a distillation tower
AU2014357667B2 (en) 2013-12-06 2017-10-05 Exxonmobil Upstream Research Company Method and system for separating a feed stream with a feed stream distribution mechanism
AU2014357665B2 (en) 2013-12-06 2017-06-22 Exxonmobil Upstream Research Company Method and device for separating a feed stream using radiation detectors
US9823016B2 (en) 2013-12-06 2017-11-21 Exxonmobil Upstream Research Company Method and system of modifying a liquid level during start-up operations
US9964034B2 (en) 2014-04-09 2018-05-08 Exxonmobil Upstream Research Company Methods for producing a fuel gas stream
SG11201705162SA (en) 2015-02-27 2017-09-28 Exxonmobil Upstream Res Co Reducing refrigeration and dehydration load for a feed stream entering a cryogenic distillation process
US10928128B2 (en) * 2015-05-04 2021-02-23 GE Oil & Gas, Inc. Preparing hydrocarbon streams for storage
EP3317240B8 (en) * 2015-05-06 2024-11-13 Sustainable Energy Solutions, Inc. Method of cryogenic purification and ethane separation
CA2994812C (en) 2015-09-18 2020-03-10 Exxonmobil Upstream Research Company Heating component to reduce solidification in a cryogenic distillation system
CA2998466C (en) 2015-09-24 2021-06-29 Exxonmobil Upstream Research Company Treatment plant for hydrocarbon gas having variable contaminant levels
US20180259251A1 (en) * 2015-12-03 2018-09-13 Shell Oil Company Method of removing co2 from a contaminated hydrocarbon stream
EP3384216B1 (en) * 2015-12-03 2019-09-25 Shell International Research Maatschappij B.V. Method of liquefying a co2 contaminated hydrocarbon-containing gas stream
CN108472574B (zh) * 2015-12-29 2022-04-29 环球油品公司 用于通过海绵吸收回收轻质烃的方法和装置
WO2017172321A1 (en) 2016-03-30 2017-10-05 Exxonmobil Upstream Research Company Self-sourced reservoir fluid for enhanced oil recovery
DE102016010515A1 (de) * 2016-08-30 2018-03-01 Linde Aktiengesellschaft Verfahren und Vorrichtung zur effektiven Strippung von teilbeladenem Waschmittel bei physikalischen Gaswäschen
WO2019113513A1 (en) 2017-12-08 2019-06-13 Baker Hughes, A Ge Company, Llc Ionic liquid based well asphaltene inhibitors and methods of using the same
US12030000B2 (en) * 2017-12-22 2024-07-09 Sustainable Energy Solutions, Llc Vessel and method for solid-liquid separation
US11447710B2 (en) * 2018-05-07 2022-09-20 8 Rivers Capital, Llc Separation of sulfurous materials
US11306267B2 (en) 2018-06-29 2022-04-19 Exxonmobil Upstream Research Company Hybrid tray for introducing a low CO2 feed stream into a distillation tower
US11378332B2 (en) 2018-06-29 2022-07-05 Exxonmobil Upstream Research Company Mixing and heat integration of melt tray liquids in a cryogenic distillation tower
EA202091413A1 (ru) 2018-07-11 2020-09-24 Бейкер Хьюз Холдингз Ллк Скважинные ингибиторы асфальтенов на основе ионной жидкости и способы их применения
US20210131613A1 (en) * 2019-10-30 2021-05-06 Exxonmobil Upstream Research Company Integration of Contaminant Separation and Regasification Systems
US11794127B2 (en) * 2020-03-30 2023-10-24 Sustainable Energy Solutions, Inc Methods and systems for separating compounds
US20230021519A1 (en) * 2021-07-23 2023-01-26 The Tisdale Group, LLC Atmospheric Water Harvester with Cryogenic System

Family Cites Families (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2996891A (en) * 1957-09-23 1961-08-22 Conch Int Methane Ltd Natural gas liquefaction cycle
US2991896A (en) * 1957-12-30 1961-07-11 Wheaton Glass Company Reinforced glass aerosol containers
GB997507A (en) * 1963-11-04 1965-07-07 Couch Internat Methane Ltd Process for the cold separation of gas mixtures
US3376709A (en) * 1965-07-14 1968-04-09 Frank H. Dickey Separation of acid gases from natural gas by solidification
US3398544A (en) * 1966-07-27 1968-08-27 Continental Oil Co Solidification of acidic components in natural gas
US3977203A (en) * 1974-03-25 1976-08-31 Kansas University Endowment Association Purification of natural gas by liquid/liquid extraction with a polar solvent
US4533372A (en) * 1983-12-23 1985-08-06 Exxon Production Research Co. Method and apparatus for separating carbon dioxide and other acid gases from methane by the use of distillation and a controlled freezing zone
US4923493A (en) * 1988-08-19 1990-05-08 Exxon Production Research Company Method and apparatus for cryogenic separation of carbon dioxide and other acid gases from methane
US5062270A (en) * 1990-08-31 1991-11-05 Exxon Production Research Company Method and apparatus to start-up controlled freezing zone process and purify the product stream
US5265428A (en) * 1990-10-05 1993-11-30 Exxon Production Research Company Bubble cap tray for melting solids and method for using same
US5451249A (en) * 1994-06-14 1995-09-19 International Fuel Cells Landfill gas treatment system
US5819555A (en) * 1995-09-08 1998-10-13 Engdahl; Gerald Removal of carbon dioxide from a feed stream by carbon dioxide solids separation
US6168768B1 (en) * 1998-01-23 2001-01-02 Exxon Research And Engineering Company Production of low sulfer syngas from natural gas with C4+/C5+ hydrocarbon recovery
US5983663A (en) * 1998-05-08 1999-11-16 Kvaerner Process Systems, Inc. Acid gas fractionation
WO2001019496A1 (en) * 1999-09-15 2001-03-22 Eickmeyer & Associates Method and composition for removing co2 and h2s from gas mixtures
US6581409B2 (en) * 2001-05-04 2003-06-24 Bechtel Bwxt Idaho, Llc Apparatus for the liquefaction of natural gas and methods related to same
AU785419B2 (en) * 2001-05-11 2007-05-03 Institut Francais Du Petrole Process for pretreating a natural gas containing acid compounds
US20030103884A1 (en) * 2001-11-30 2003-06-05 The Regents Of The University Of California Low-emission method of recovering sulfur from sour industrial gases
NZ534723A (en) * 2002-01-18 2004-10-29 Univ Curtin Tech Process and device for production of LNG by removal of freezable solids
AU2003900534A0 (en) * 2003-02-07 2003-02-20 Shell Internationale Research Maatschappij B.V. Process and apparatus for removal of a contaminant from a natural gas feed stream

Also Published As

Publication number Publication date
WO2007030888A1 (en) 2007-03-22
US20100147022A1 (en) 2010-06-17
EA012227B1 (ru) 2009-08-28
EP1931755A1 (en) 2008-06-18
CN101283078A (zh) 2008-10-08
CA2622570A1 (en) 2007-03-22
AU2010201570A1 (en) 2010-05-13
AU2006291954A1 (en) 2007-03-22
EP1931755A4 (en) 2011-08-03
NZ566742A (en) 2010-07-30
MY145090A (en) 2011-12-30
AU2006291954C1 (en) 2014-01-09
AU2006291954B2 (en) 2010-01-21

Similar Documents

Publication Publication Date Title
EA200800827A1 (ru) Способ и устройство для удаления кислых веществ из потока природного газа
EA201100181A1 (ru) Способ удаления газообразного загрязнителя из потока загрязнённого газа
EA201891653A1 (ru) Разделение нефти, воды, газа и твердых частиц при добыче нефти и/или газа
EA201300407A1 (ru) Способ отделения жидкости от суспендированного вещества в отстое и устройство для осуществления способа
UA107956C2 (en) Compact concentrator wastewater and scrubber
EA200870151A1 (ru) Способ и реактор для анаэробной очистки сточных вод
EA200601957A1 (ru) Удаление загрязнителей из природного газа с помощью охлаждения
WO2010019282A3 (en) Mercury removal from crude oil
MY150792A (en) System and method for removing hydrogen sulfide from a natural gas stream
EA201070743A1 (ru) Система и способ отделения углеводородов
WO2008045253A3 (en) Compact multiphase inline bulk water separation method and system for hydrocarbon production
EA200870468A1 (ru) Система для обработки текучей среды и способ использования этой системы
US20180236397A1 (en) Hydrocyclone For Cryogenic Gas-Vapor Separation
RU2016134044A (ru) Фильтрация через различные стратифицированные материалы
EA200801246A1 (ru) Способ разделения смеси и установка для разделения смеси, содержащей воду, нефть и газ
ATE455163T1 (de) Verfahren zur entwässerung eines in einem vergasungsverfahren bekommenen russ-wasser- schlamms
CL2013002530A1 (es) Aparato para tratamiento de gas de sintesis bruto generado por gasificacion subterranea de carbon ucg, que comprende un separador de liquidos y solidos que contiene una vasija y un filtro de cesta alojado dentro de la seccion de fondo de la vasija, y un sistema de ventilacion; separador, metodo para separar liquidos y solidos del gas de sintesis.
MXPA04001895A (es) Deshidratador de aceite.
EA201170195A1 (ru) Устройство очистки масляных паров
EA201190040A1 (ru) Активация катализатора в процессах фишера-тропша
EA015894B1 (ru) Флотационное устройство
RU2501594C1 (ru) Способ подготовки сероводород- и меркаптансодержащей нефти
CN203890156U (zh) 平台污水净化装置
JP2014000561A (ja) ガス＆ガス混合等乱流接触による球形サイクロンの方法とその装置。
RU2469774C1 (ru) Установка очистки сжиженных углеводородных газов от кислых компонентов

Legal Events

Date Code Title Description
MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): AM BY KG MD TJ

PC4A Registration of transfer of a eurasian patent by assignment
MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): AZ KZ TM