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AR078438A1 - Sistema criogenico para la eliminacion de gases acidos de una corriente de gas de hidrocarburos, con eliminacion de sulfuro de hidrogeno - Google Patents

Sistema criogenico para la eliminacion de gases acidos de una corriente de gas de hidrocarburos, con eliminacion de sulfuro de hidrogeno

Info

Publication number
AR078438A1
AR078438A1 ARP100103467A ARP100103467A AR078438A1 AR 078438 A1 AR078438 A1 AR 078438A1 AR P100103467 A ARP100103467 A AR P100103467A AR P100103467 A ARP100103467 A AR P100103467A AR 078438 A1 AR078438 A1 AR 078438A1
Authority
AR
Argentina
Prior art keywords
elimination
gas stream
scrs
hydrogen sulfide
stream
Prior art date
Application number
ARP100103467A
Other languages
English (en)
Original Assignee
Exxonmobil Upstream Res Co
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 Exxonmobil Upstream Res Co filed Critical Exxonmobil Upstream Res Co
Publication of AR078438A1 publication Critical patent/AR078438A1/es

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/0204Processes 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
    • F25J3/0209Natural gas or substitute natural gas
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10Working-up natural gas or synthetic natural gas
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10Working-up natural gas or synthetic natural gas
    • C10L3/101Removal of contaminants
    • C10L3/102Removal of contaminants of acid contaminants
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/0228Processes 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
    • F25J3/0233Processes 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/0228Processes 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
    • F25J3/0266Processes 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/0295Start-up or control of the process; Details of the apparatus used, e.g. sieve plates, packings
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/74Refluxing the column with at least a part of the partially condensed overhead gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/76Refluxing the column with condensed overhead gas being cycled in a quasi-closed loop refrigeration cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/90Details relating to column internals, e.g. structured packing, gas or liquid distribution
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2205/00Processes or apparatus using other separation and/or other processing means
    • F25J2205/02Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
    • F25J2205/04Processes 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2205/00Processes or apparatus using other separation and/or other processing means
    • F25J2205/40Processes or apparatus using other separation and/or other processing means using hybrid system, i.e. combining cryogenic and non-cryogenic separation techniques
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2205/00Processes or apparatus using other separation and/or other processing means
    • F25J2205/50Processes 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2205/00Processes or apparatus using other separation and/or other processing means
    • F25J2205/60Processes or apparatus using other separation and/or other processing means using adsorption on solid adsorbents, e.g. by temperature-swing adsorption [TSA] at the hot or cold end
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2205/00Processes or apparatus using other separation and/or other processing means
    • F25J2205/60Processes or apparatus using other separation and/or other processing means using adsorption on solid adsorbents, e.g. by temperature-swing adsorption [TSA] at the hot or cold end
    • F25J2205/66Regenerating the adsorption vessel, e.g. kind of reactivation gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2215/00Processes characterised by the type or other details of the product stream
    • F25J2215/04Recovery of liquid products
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2220/00Processes or apparatus involving steps for the removal of impurities
    • F25J2220/60Separating impurities from natural gas, e.g. mercury, cyclic hydrocarbons
    • F25J2220/66Separating acid gases, e.g. CO2, SO2, H2S or RSH
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2260/00Coupling of processes or apparatus to other units; Integrated schemes
    • F25J2260/80Integration in an installation using carbon dioxide, e.g. for EOR, sequestration, refrigeration etc.
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2270/00Refrigeration techniques used
    • F25J2270/90External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2280/00Control of the process or apparatus
    • F25J2280/40Control of freezing of components
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02CCAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00Capture or disposal of greenhouse gases
    • Y02C20/40Capture or disposal of greenhouse gases of CO2

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Gas Separation By Absorption (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

Un sistema para la eliminacion de gases ácidos de una corriente de gas crudo incluye un sistema de eliminacion de gases ácidos (AGRS, segun su sigla en inglés) y un sistema de eliminacion de componentes sulfurosos (SCRS, segun su sigla en inglés). El sistema de eliminacion de gas ácido recibe una corriente de gas amargo y la separa en una corriente de gas superior compuesta principalmente por metano, y una corriente de gas ácido inferior compuesta principalmente por dioxido de carbono. El sistema de eliminacion de componentes sulfurosos se coloca o bien corriente ascendente o corriente descendente del sistema de eliminacion de gases ácidos. El SCRS recibe una corriente de gas y separa generalmente la corriente de gas en una primera corriente de fluido que comprende sulfuro de hidrogeno, y una segunda corriente de fluido que comprende dioxido de carbono. Cuando el SCRS se encuentra corriente ascendente del AGRS, la segunda corriente de fluido además comprende principalmente metano. Cuando el SCRS se encuentra corriente descendente del AGRS, la segunda corriente de fluido es principalmente dioxido de carbono. Pueden utilizarse diversos tipos de sistemas de eliminacion de componentes sulfurosos.
ARP100103467A 2009-11-02 2010-09-23 Sistema criogenico para la eliminacion de gases acidos de una corriente de gas de hidrocarburos, con eliminacion de sulfuro de hidrogeno AR078438A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US25727709P 2009-11-02 2009-11-02

Publications (1)

Publication Number Publication Date
AR078438A1 true AR078438A1 (es) 2011-11-09

Family

ID=43922440

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP100103467A AR078438A1 (es) 2009-11-02 2010-09-23 Sistema criogenico para la eliminacion de gases acidos de una corriente de gas de hidrocarburos, con eliminacion de sulfuro de hidrogeno

Country Status (13)

Country Link
US (1) US20120204599A1 (es)
EP (1) EP2496901A4 (es)
JP (1) JP2013509300A (es)
CN (1) CN102597671B (es)
AR (1) AR078438A1 (es)
AU (1) AU2010313733B2 (es)
BR (1) BR112012009867A2 (es)
CA (1) CA2777760C (es)
EA (1) EA023174B1 (es)
MX (1) MX337923B (es)
MY (1) MY159666A (es)
SG (1) SG10201407019PA (es)
WO (1) WO2011053400A1 (es)

Families Citing this family (81)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EA021006B1 (ru) 2009-04-20 2015-03-31 Эксонмобил Апстрим Рисерч Компани Способ удаления кислотных газов из потока углеводородного газа
CN102905772A (zh) 2010-02-17 2013-01-30 氟石科技公司 在制备超低硫气体中清除高压酸气体的构造和方法
GB2507233B (en) * 2011-08-09 2019-07-10 Exxonmobil Upstream Res Co Natural gas liquefaction process
CA2772479C (en) 2012-03-21 2020-01-07 Mackenzie Millar Temperature controlled method to liquefy gas and a production plant using the method.
AU2013235610B2 (en) 2012-03-21 2015-11-19 Exxonmobil Upstream Research Company Separating carbon dioxide and ethane from a mixed stream
CA2790961C (en) 2012-05-11 2019-09-03 Jose Lourenco A method to recover lpg and condensates from refineries fuel gas streams.
EP2685189A1 (en) * 2012-07-13 2014-01-15 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Process for storing liquid rich in carbon dioxide in solid form
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
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
MX368367B (es) 2013-01-25 2019-09-30 Exxonmobil Upstream Res Co Contacto de una corriente de gas con una corriente de liquido.
CA2813260C (en) 2013-04-15 2021-07-06 Mackenzie Millar A method to produce lng
AR096078A1 (es) 2013-05-09 2015-12-02 Exxonmobil Upstream Res Co Separación de impurezas de una corriente de gas usando un sistema de contacto en equicorriente orientado verticalmente
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
RU2522155C1 (ru) * 2013-07-04 2014-07-10 Андрей Владиславович Курочкин Сверхкритический сепаратор
EP3046653B1 (en) * 2013-09-16 2020-10-28 Savannah River Nuclear Solutions, LLC Mass transfer apparatus and method for separation of gases
US9764272B2 (en) * 2013-10-28 2017-09-19 Energy Recovery, Inc. Systems and methods for utilizing turbine systems within gas processing systems
CA2924402C (en) 2013-12-06 2017-11-21 Exxonmobil Upstream Research Company Method and device for separating a feed stream using radiation detectors
WO2015084495A2 (en) * 2013-12-06 2015-06-11 Exxonmobil Upstream Research Company Method and system of maintaining a liquid level 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
CA2924695C (en) * 2013-12-06 2018-10-02 Exxonmobil Upstream Research Company Method and system for separating a feed stream with a feed stream distribution mechanism
WO2015084499A2 (en) 2013-12-06 2015-06-11 Exxonmobil Upstream Research Company Method and system of modifying a liquid level during start-up operations
US9874395B2 (en) 2013-12-06 2018-01-23 Exxonmobil Upstream Research Company Method and system for preventing accumulation of solids in a distillation tower
MY177768A (en) 2013-12-06 2020-09-23 Exxonmobil Upstream Res Co Method and device for separating hydrocarbons and contaminants with a heating mechanism to destabilize and/or prevent adhesion of solids
AU2014357663B2 (en) 2013-12-06 2016-12-22 Exxonmobil Upstream Research Company Method and device for separating hydrocarbons and contaminants with a spray assembly
WO2015089446A1 (en) 2013-12-12 2015-06-18 Fluor Technologies Corporation Configurations and methods of flexible co2 removal
US9504984B2 (en) * 2014-04-09 2016-11-29 Exxonmobil Upstream Research Company Generating elemental sulfur
WO2015163997A2 (en) 2014-04-22 2015-10-29 Exxonmobil Upstream Research Company Method and system for starting up a distillation tower
MY183001A (en) 2014-06-11 2021-02-05 Exxonmobil Upstream Res Co Method for separating a feed gas in a column
US9739529B2 (en) 2014-07-08 2017-08-22 Exxonmobil Upstream Research Company Method and system for separating fluids in a distillation tower
WO2016023098A1 (en) 2014-08-15 2016-02-18 1304338 Alberta Ltd. A method of removing carbon dioxide during liquid natural gas production from natural gas at gas pressure letdown stations
US9823017B2 (en) 2014-10-22 2017-11-21 Exxonmobil Upstream Research Company Method and system of controlling a temperature within a melt tray assembly of a distillation tower
CA2966991C (en) 2014-11-17 2019-04-09 Exxonmobil Upstream Research Company Heat exchange mechanism for removing contaminants from a hydrocarbon vapor stream
AU2015374634B2 (en) 2014-12-30 2018-05-31 Exxonmobil Upstream Research Company Accumulation and melt tray assembly for a distillation tower
CN107106969B (zh) 2015-01-09 2020-03-03 埃克森美孚上游研究公司 使用多个同流接触器从流体流分离杂质
KR101964584B1 (ko) 2015-02-17 2019-04-03 엑손모빌 업스트림 리서치 캄파니 병류 컨택터에 대한 내부 표면 특징
RU2576934C1 (ru) * 2015-02-24 2016-03-10 Андрей Владиславович Курочкин Фракционирующий холодильник-конденсатор
US10495379B2 (en) 2015-02-27 2019-12-03 Exxonmobil Upstream Research Company Reducing refrigeration and dehydration load for a feed stream entering a cryogenic distillation process
WO2016148780A1 (en) 2015-03-13 2016-09-22 Exxonmobil Upstream Research Company Coalescer for co-current contactors
WO2016209404A1 (en) 2015-06-22 2016-12-29 Exxonmobil Upstream Research Company Purge to intermediate pressure in cryogenic distillation
US9808755B2 (en) * 2015-07-24 2017-11-07 Air Products And Chemicals, Inc. Sour pressure swing adsorption process
CN108431184B (zh) * 2015-09-16 2021-03-30 1304342阿尔伯塔有限公司 在气体减压站制备天然气以生产液体天然气(lng)的方法
CA2994812C (en) 2015-09-18 2020-03-10 Exxonmobil Upstream Research Company Heating component to reduce solidification in a cryogenic distillation system
US10569219B2 (en) 2015-09-21 2020-02-25 Exxonmobil Upstream Research Company Systems and methods for separating hydrogen sulfide from carbon dioxide in a high-pressure mixed stream
CA2998466C (en) * 2015-09-24 2021-06-29 Exxonmobil Upstream Research Company Treatment plant for hydrocarbon gas having variable contaminant levels
CN106608618A (zh) * 2015-10-21 2017-05-03 中国石油化工股份有限公司 酸气净化工艺
BR112018008451A2 (pt) * 2015-10-27 2018-12-11 Fluor Tech Corp configurações e métodos para processar gases ácidos de alta pressão sem emissões
US10173389B2 (en) * 2015-12-15 2019-01-08 Bloom Energy Corporation Carbon dioxide shielded natural gas line and method of using thereof
WO2017143215A1 (en) * 2016-02-19 2017-08-24 Exxonmobil Upstream Reasrch Company Cold solvent gas treating system for selective h2s removal
EA201892054A1 (ru) 2016-03-30 2019-02-28 Эксонмобил Апстрим Рисерч Компани Поступающая из собственных источников пластовая текучая среда для повышения нефтеотдачи
CN105771539A (zh) * 2016-03-31 2016-07-20 四川天采科技有限责任公司 一种适用于炼厂的高浓度硫化氢尾气的脱除工艺
US11634651B2 (en) * 2016-09-08 2023-04-25 Waste to Energy Systems, LLC System and method for biogasification
US10539364B2 (en) * 2017-03-13 2020-01-21 General Electric Company Hydrocarbon distillation
CN107051125A (zh) * 2017-05-03 2017-08-18 海湾环境科技(北京)股份有限公司 油气回收系统
CN110740795B (zh) 2017-06-15 2022-02-25 埃克森美孚上游研究公司 使用成束的紧凑并流接触系统的分馏系统
US11000795B2 (en) 2017-06-15 2021-05-11 Exxonmobil Upstream Research Company Fractionation system using compact co-current contacting systems
US10876052B2 (en) 2017-06-20 2020-12-29 Exxonmobil Upstream Research Company Compact contacting systems and methods for scavenging sulfur-containing compounds
AU2018322436B2 (en) 2017-08-21 2021-07-22 Exxonmobil Upstream Research Company Integration of cold solvent and acid gas removal
CN107880946B (zh) * 2017-12-13 2023-05-16 中冶焦耐(大连)工程技术有限公司 一种煤气冷却分离装置及方法
US20190194551A1 (en) * 2017-12-22 2019-06-27 Clariant International, Ltd. Synergized acetals composition and method for scavenging sulfides and mercaptans
WO2019195570A1 (en) * 2018-04-06 2019-10-10 Baker Hughes, A Ge Company, Llc In-line pipe contactor
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
WO2020005553A1 (en) 2018-06-29 2020-01-02 Exxonmobil Upstream Research Company (Emhc-N1.4A.607) Mixing and heat integration of melt tray liquids in a cryogenic distillation tower
CN108744565B (zh) * 2018-07-31 2023-07-14 中国大唐集团科学技术研究院有限公司西北分公司 一种蒸发结晶换热装置与燃煤厂脱硫废水零排放系统
EP3616774A1 (de) * 2018-09-03 2020-03-04 L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude Verfahren und vorrichtung zur abtrennung von metallcarbonylen aus einem gasgemisch
CN109387030B (zh) * 2018-11-17 2023-08-01 杭州宏盛中弘新能源有限公司 一种低浓度煤矿瓦斯液化提浓甲烷制lng的系统及方法
WO2020205750A1 (en) 2019-03-29 2020-10-08 Bright Energy Storage Technologies, Llp Co2 separation & liquefaction system and method
RU2723874C1 (ru) * 2019-11-21 2020-06-17 Сергей Леонидович Терентьев Установка десорбции (испарения) с глубокой рекуперацией тепла
CN111760546A (zh) * 2020-07-13 2020-10-13 江西庞泰环保股份有限公司 一种气液分布支撑平衡装置
US11745136B2 (en) 2020-10-14 2023-09-05 Bcck Holding Company System and method for treating a methane system to remove carbon dioxide, hydrogen sulfide, and water in a single process
RU2761705C1 (ru) * 2021-04-13 2021-12-13 федеральное государственное бюджетное образовательное учреждение высшего образования "Нижегородский государственный технический университет им. Р.Е. Алексеева" (НГТУ) Способ удаления диоксида углерода из природного газа
CN115691688A (zh) * 2021-07-30 2023-02-03 中国石油化工股份有限公司 一种酸性气体中硫溶解行为的分子模拟方法及其应用
CN113491883B (zh) * 2021-08-12 2022-06-28 江西全兴化工填料有限公司 用于分离可燃性气体的金属填料分馏塔
AU2022390169A1 (en) * 2021-11-18 2024-06-27 Dvo Licensing, Inc. Method and apparatus for anaerobic digestion of liquid waste streams
CN114272724B (zh) * 2021-12-31 2024-04-02 南京亿碳科技有限公司 一种新型节能co2回收装置
CN114653184B (zh) * 2022-04-01 2023-10-27 北京建筑大学 一种去除恶臭气体和生物气溶胶的系统和方法
US11629571B1 (en) * 2022-12-05 2023-04-18 Capwell Seavices Llc Modular well capping system, kit, and methods
GB202302933D0 (en) * 2023-02-28 2023-04-12 Caloritum Nv System and method preventing leakage from industrial equipment operating in corrosive environments
CN116731760B (zh) * 2023-07-20 2024-01-02 北京化工大学 一种低浓度煤层气气水合物法循环提纯系统
CN117553516A (zh) * 2023-12-29 2024-02-13 江苏正丹化学工业股份有限公司 一种偏三甲苯连续氧化尾气制氮生产装置
CN118256334B (zh) * 2024-05-30 2025-06-24 山东中创健康科技集团有限公司 微生物添加剂发酵空气多级过滤除菌装置

Family Cites Families (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4222991A (en) * 1978-05-18 1980-09-16 Union Oil Company Of California Process for removing SOx and NOx compounds from gas streams
US4370156A (en) * 1981-05-29 1983-01-25 Standard Oil Company (Indiana) Process for separating relatively pure fractions of methane and carbon dioxide from gas mixtures
US4459142A (en) * 1982-10-01 1984-07-10 Standard Oil Company (Indiana) Cryogenic distillative removal of CO2 from high CO2 content hydrocarbon containing streams
CA1219731A (en) * 1983-05-02 1987-03-31 John Happel Process for desulfurizing fuel gases
US4563202A (en) * 1984-08-23 1986-01-07 Dm International Inc. Method and apparatus for purification of high CO2 content gas
US4831206A (en) * 1987-03-05 1989-05-16 Uop Chemical processing with an operational step sensitive to a feedstream component
EP0398952A4 (en) * 1988-01-15 1991-05-22 Chevron Research Company Composition, method and apparatus for removal of hydrogen sulfide
US4874524A (en) * 1988-03-30 1989-10-17 The Curators Of The University Of Missouri Separation of adsorbed components by variable temperature desorption
DE3828227A1 (de) * 1988-08-19 1990-02-22 Basf Ag Verfahren zum entfernen von co(pfeil abwaerts)2(pfeil abwaerts) und gegebenenfalls h(pfeil abwaerts)2(pfeil abwaerts) aus gasen
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
US5120338A (en) * 1991-03-14 1992-06-09 Exxon Production Research Company Method for separating a multi-component feed stream using distillation and controlled freezing zone
US5126118A (en) * 1991-04-08 1992-06-30 Ari Technologies, Inc. Process and apparatus for removal of H2 S with separate absorber and oxidizer and a reaction chamber therebetween
CA2133302A1 (en) * 1993-10-06 1995-04-07 Ravi Kumar Integrated process for purifying and liquefying a feed gas mixture with respect to its less strongly adsorbed component of lower volatility
DE19704173C1 (de) * 1997-02-05 1998-04-16 Webasto Karosseriesysteme Flexibles Verdeck eines Fahrzeugs
ID24280A (id) * 1997-07-01 2000-07-13 Exxon Production Research Co Proses untuk memisahkan aliran gas multi-komponen yang mengandung paling tidak satu komponen yang dapat membeku
TW366409B (en) * 1997-07-01 1999-08-11 Exxon Production Research Co Process for liquefying a natural gas stream containing at least one freezable component
US6416729B1 (en) * 1999-02-17 2002-07-09 Crystatech, Inc. Process for removing hydrogen sulfide from gas streams which include or are supplemented with sulfur dioxide
GB0015997D0 (en) * 2000-06-29 2000-08-23 Norske Stats Oljeselskap Method for mixing fluids
GB0031710D0 (en) * 2000-12-27 2001-02-07 Dyno Oil Field Chemicals Process for the reduction or elimination of hydrogen sulphide
FR2848121B1 (fr) * 2002-12-04 2005-01-28 Inst Francais Du Petrole Procede de traitement d'un gaz naturel acide
JP2005097542A (ja) * 2003-08-28 2005-04-14 Kobe Steel Ltd 炭化水素含有ガス処理装置および炭化水素含有ガス処理方法
PL2402068T5 (pl) * 2004-01-20 2017-09-29 Fluor Tech Corp Sposoby i konfiguracje do wzbogacania gazu kwaśnego
CA2583120C (en) * 2004-12-03 2014-03-25 Exxonmobil Upstream Research Company Integrated acid gas and sour gas reinjection process
US20100018248A1 (en) * 2007-01-19 2010-01-28 Eleanor R Fieler Controlled Freeze Zone Tower
US20080256977A1 (en) * 2007-04-20 2008-10-23 Mowrey Earle R Hydrocarbon recovery and light product purity when processing gases with physical solvents
US8529664B2 (en) * 2007-05-18 2013-09-10 Exxonmobil Research And Engineering Company Removal of a target gas from a mixture of gases by swing adsorption with use of a turboexpander
JP2010536573A (ja) * 2007-08-30 2010-12-02 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ 酸ガス流からの硫化水素及び二酸化炭素の除去方法
US20090090049A1 (en) * 2007-10-09 2009-04-09 Chevron U.S.A. Inc. Process for producing liqefied natural gas from high co2 natural gas
US20090220406A1 (en) * 2008-02-29 2009-09-03 Greatpoint Energy, Inc. Selective Removal and Recovery of Acid Gases from Gasification Products
US7955496B2 (en) * 2008-04-22 2011-06-07 Kellogg Brown & Root Llc Systems and methods for upgrading hydrocarbons

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