EA201791077A1 - Теплообменный механизм для удаления загрязнения из потока паров углеводородов - Google Patents

Теплообменный механизм для удаления загрязнения из потока паров углеводородов

Info

Publication number
EA201791077A1
EA201791077A1 EA201791077A EA201791077A EA201791077A1 EA 201791077 A1 EA201791077 A1 EA 201791077A1 EA 201791077 A EA201791077 A EA 201791077A EA 201791077 A EA201791077 A EA 201791077A EA 201791077 A1 EA201791077 A1 EA 201791077A1
Authority
EA
Eurasian Patent Office
Prior art keywords
flow
solids
hydrocarbon
heat exchange
exchange mechanism
Prior art date
Application number
EA201791077A
Other languages
English (en)
Inventor
Николас Ф. Урбански
Original Assignee
Эксонмобил Апстрим Рисерч Компани
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 Эксонмобил Апстрим Рисерч Компани filed Critical Эксонмобил Апстрим Рисерч Компани
Publication of EA201791077A1 publication Critical patent/EA201791077A1/ru

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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/008Liquid distribution
    • 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • 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
    • 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • 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
    • 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/06Heat exchange, direct or indirect
    • 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/54Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
    • C10L2290/543Distillation, fractionation or rectification for separating fractions, components or impurities during preparation or upgrading of a fuel
    • 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
    • F25J2200/02Processes or apparatus using separation by rectification in a single pressure main column system
    • 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
    • F25J2200/30Processes or apparatus using separation by rectification using a side column in a single pressure column system
    • 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
    • F25J2200/50Processes or apparatus using separation by rectification using multiple (re-)boiler-condensers at different heights of the column
    • 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
    • F25J2200/90Details 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
    • F25J2205/20Processes or apparatus using other separation and/or other processing means using solidification of components
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Система для плавления содержащих загрязнители твердых веществ, которые были отделены от содержащего углеводород парового потока в углеводородной дистилляционной колонне, содержащей по меньшей мере одну пластину, размещаемую там, где формируются твердые вещества в пределах углеводородной дистилляционной колонны, полый трубопровод, формирующий неотъемлемую часть каждой по меньшей мере одной пластины, и нагревающую среду, помещенную для течения через полый трубопровод при более высокой температуре, чем температура твердых веществ, по меньшей мере, для частичного плавления твердых веществ.
EA201791077A 2014-11-17 2015-09-09 Теплообменный механизм для удаления загрязнения из потока паров углеводородов EA201791077A1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201462080450P 2014-11-17 2014-11-17
PCT/US2015/049107 WO2016081051A1 (en) 2014-11-17 2015-09-09 Heat exchange mechanism for removing contaminants from a hydrocarbon vapor stream

Publications (1)

Publication Number Publication Date
EA201791077A1 true EA201791077A1 (ru) 2017-12-29

Family

ID=54207730

Family Applications (1)

Application Number Title Priority Date Filing Date
EA201791077A EA201791077A1 (ru) 2014-11-17 2015-09-09 Теплообменный механизм для удаления загрязнения из потока паров углеводородов

Country Status (9)

Country Link
US (2) US10281205B2 (ru)
CN (1) CN106999792B (ru)
AR (1) AR102607A1 (ru)
AU (1) AU2015350515B2 (ru)
CA (1) CA2966991C (ru)
EA (1) EA201791077A1 (ru)
MX (1) MX2017005037A (ru)
SG (1) SG11201702747VA (ru)
WO (1) WO2016081051A1 (ru)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107208964B (zh) * 2015-02-27 2020-06-19 埃克森美孚上游研究公司 减少进入低温蒸馏过程的进料物流的冷冻和脱水负荷
RU2636966C1 (ru) * 2016-11-14 2017-11-29 Федеральное государственное бюджетное образовательное учреждение высшего образования "Уфимский государственный нефтяной технический университет" Способ производства сжиженного природного газа
US10961480B2 (en) 2017-01-17 2021-03-30 Exxonmobil Chemical Patents Inc. High stability lubricating oil base stocks and processes for preparing the same
US20190170440A1 (en) * 2017-12-05 2019-06-06 Larry Baxter Pressure-Regulated Melting of Solids
US20190170441A1 (en) * 2017-12-05 2019-06-06 Larry Baxter Pressure-Regulated Melting of Solids with Warm Fluids
US10786751B2 (en) * 2018-05-08 2020-09-29 Process Consulting Services, Inc. Coker fractionator spray wash chamber
US11345862B2 (en) * 2019-11-07 2022-05-31 Indian Oil Corporation Limited Apparatus and a method for washing of hydrocarbon product vapor

Family Cites Families (56)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1510178A (en) 1921-01-03 1924-09-30 Lachmann Walter Rectifying column
US2347957A (en) * 1939-06-17 1944-05-02 William E Mccullough Heat exchange unit
US2502251A (en) 1946-12-13 1950-03-28 Air Reduction Apparatus for the separation of gaseous mixtures
US2650480A (en) 1947-08-22 1953-09-01 Phillips Petroleum Co Low-temperature absorption refrigeration
US2804292A (en) 1949-02-02 1957-08-27 Air Prod Inc Gas-liquid contact apparatus
US2930201A (en) 1953-08-31 1960-03-29 Linde Eismasch Ag Process for the production of oxygen of low argon content
US2946200A (en) 1955-06-09 1960-07-26 Air Prod Inc Method of separating gaseous mixtures
US4071934A (en) * 1975-10-17 1978-02-07 Brazeway, Inc. CFT Box fin
FR2542421B1 (fr) 1983-03-08 1985-07-05 Air Liquide Procede et appareil pour produire un gaz a haute purete par vaporisation d'un liquide cryogenique
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
US4708199A (en) * 1985-02-28 1987-11-24 Kabushiki Kaisha Tsuchiya Seisakusho Heat exchanger
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
US5052270A (en) 1990-06-20 1991-10-01 The United States Of America As Represented By The Secretary Of The Navy Multi-sonobuoy launch container with constant force spring
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
US5122174A (en) * 1991-03-01 1992-06-16 Air Products And Chemicals, Inc. Boiling process and a heat exchanger for use in the process
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
US5758720A (en) * 1996-11-26 1998-06-02 Behr America, Inc. Unitary heat exchanger core and method of making same
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
WO1999001707A1 (en) 1997-07-01 1999-01-14 Exxon Production Research Company Process for separating a multi-component gas stream containing at least one freezable component
EP0906796A1 (en) 1997-10-01 1999-04-07 Norsk Hydro Asa Process for making a heat exchanger
DE10106371A1 (de) 2001-02-12 2002-08-14 Ludwig Pilsl Vorrichtung für den Austausch von Wärme
JP2003090690A (ja) * 2001-09-18 2003-03-28 Hitachi Ltd 積層型熱交換器及び冷凍サイクル
US6834515B2 (en) * 2002-09-13 2004-12-28 Air Products And Chemicals, Inc. Plate-fin exchangers with textured surfaces
WO2006062595A1 (en) 2004-12-03 2006-06-15 Exxonmobil Upstream Research Company Corp-Urc-Sw348 Integrated acid gas and sour gas reinjection process
US20100018248A1 (en) * 2007-01-19 2010-01-28 Eleanor R Fieler Controlled Freeze Zone Tower
AU2007345353B2 (en) * 2007-01-19 2013-02-21 Exxonmobil Upstream Research Company Integrated controlled freeze zone (CFZ) tower and dividing wall (DWC) for enhanced hydrocarbon recovery
JP5490685B2 (ja) * 2007-06-07 2014-05-14 デカ・プロダクツ・リミテッド・パートナーシップ 水蒸気蒸留の装置、方法およびシステム
AU2009330799B2 (en) 2008-12-22 2016-04-21 Twister B.V. Method of removing carbon dioxide from a fluid stream and fluid separation assembly
AU2010239718B2 (en) 2009-04-20 2016-02-04 Exxonmobil Upstream Research Company Cryogenic system for removing acid gases from a hyrdrocarbon gas stream, and method of removing acid gases
US20110024080A1 (en) * 2009-07-29 2011-02-03 Prodigy Energy Recovery Systems, Inc. Heat Exchanger
EP2459505A4 (en) 2009-07-30 2013-04-17 Exxonmobil Upstream Res Co SYSTEMS AND METHODS FOR REMOVING HEAVY HYDROCARBONS AND ACIDIC GAS FROM A HYDROCARBON GAS CURRENT
AU2010307274B2 (en) * 2009-09-09 2016-02-18 Exxonmobil Upstream Research Company Cryogenic system for removing acid gasses from a hydrocarbon gas stream
AU2010313733B2 (en) 2009-11-02 2016-05-12 Exxonmobil Upstream Research Company Cryogenic system for removing acid gases from a hydrocarbon gas stream, with removal of hydrogen sulfide
MY161559A (en) 2010-01-22 2017-04-28 Exxonmobil Upstream Res Co Removal of acid gases from a gas stream, with co2 capture and sequestration
CA2786498C (en) 2010-02-03 2018-06-26 Exxonmobil Upstream Research Company Systems and methods for using cold liquid to remove solidifiable gas components from process gas streams
US8585802B2 (en) 2010-07-09 2013-11-19 Arnold Keller Carbon dioxide capture and liquefaction
MX362706B (es) 2010-07-30 2019-02-01 Exxonmobil Upstream Res Company Star Sistemas criogenicos para remover gases acidos de una corriente de gas de hidrocarburo que usan dispositivos de separacion de co-corriente.
RU2606223C2 (ru) 2011-07-22 2017-01-10 Эксонмобил Апстрим Рисерч Компани Извлечение гелия из потоков природного газа
WO2013095828A1 (en) 2011-12-20 2013-06-27 Exxonmobil Upstream Research Company Method of separating carbon dioxide from liquid acid gas streams
US9964352B2 (en) 2012-03-21 2018-05-08 Exxonmobil Upstream Research Company Separating carbon dioxide and ethane from a mixed stream
EP2685191A1 (en) 2012-07-13 2014-01-15 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Process and apparatus for the separation of a gas rich in carbon dioxide
WO2015084495A2 (en) 2013-12-06 2015-06-11 Exxonmobil Upstream Research Company Method and system of maintaining a liquid level in a distillation tower
US10139158B2 (en) 2013-12-06 2018-11-27 Exxonmobil Upstream Research Company Method and system for separating a feed stream with a feed stream distribution mechanism
MX363766B (es) 2013-12-06 2019-04-02 Exxonmobil Upstream Res Co Metodo y dispositivo para separar hidrocarburos y contaminantes con un mecanismo de calentamiento para desestabilizar y/o prevenir la adhesion de solidos.
US20150159942A1 (en) 2013-12-06 2015-06-11 Jaime A. Valencia Method and device for separating hydrocarbons and contaminants with a surface treatment mechanism
WO2015084494A2 (en) 2013-12-06 2015-06-11 Exxonmobil Upstream Research Company Method and device for separating hydrocarbons and contaminants with a spray assembly
MY177751A (en) 2013-12-06 2020-09-23 Exxonmobil Upstream Res Co Method and device for separating a feed stream using radiation detectors
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
AU2014357668B2 (en) 2013-12-06 2017-05-25 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
MY183946A (en) 2013-12-06 2021-03-17 Exxonmobil Upstream Res Co Method and system of dehydrating a feed stream processed in a distillation tower
US9504984B2 (en) 2014-04-09 2016-11-29 Exxonmobil Upstream Research Company Generating elemental sulfur
US9739528B2 (en) 2014-04-22 2017-08-22 Exxonmobil Upstream Research Company Method and system for starting up a distillation tower
US9784498B2 (en) 2014-06-11 2017-10-10 Exxonmobil Upstream Research Company Method for separating a feed gas in a column
WO2016007209A1 (en) 2014-07-08 2016-01-14 Exxonmobil Upstream Research Company Method and system for separating fluids in a distillation tower

Also Published As

Publication number Publication date
AR102607A1 (es) 2017-03-15
CA2966991A1 (en) 2016-05-26
SG11201702747VA (en) 2017-06-29
CN106999792A (zh) 2017-08-01
WO2016081051A1 (en) 2016-05-26
US20190219328A1 (en) 2019-07-18
AU2015350515A1 (en) 2017-06-01
MX2017005037A (es) 2017-06-30
CA2966991C (en) 2019-04-09
CN106999792B (zh) 2019-11-12
US11543179B2 (en) 2023-01-03
AU2015350515B2 (en) 2018-11-15
US20160138863A1 (en) 2016-05-19
US10281205B2 (en) 2019-05-07

Similar Documents

Publication Publication Date Title
EA201791077A1 (ru) Теплообменный механизм для удаления загрязнения из потока паров углеводородов
RU2014107329A (ru) Башня мокрого тушения для тушения горячего кокса
JP2016530096A5 (ru)
EA201990597A1 (ru) Системы и способы регулирования добычи углеводородов
EA201691170A1 (ru) Способ и устройство для разделения углеводородов и загрязняющих примесей с помощью нагревательного устройства для дестабилизации и/или предотвращения адгезии твердых веществ
CL2017003262A1 (es) Sistema y método para el tratamiento térmico del cieno
EA201490299A1 (ru) Способ удаления примесей из конденсата топочного газа
PE20161535A1 (es) Procedimiento para producir hidrogeno
RU2014153605A (ru) Способ модернизации действующей установки низкотемпературной сепарации газа
SA517381667B1 (ar) أنابيب فرن تحلل حراري
EA201791479A1 (ru) Тарельчатый узел для сбора и расплавления, предназначенный для дистилляционной колонны
BR112017011138A2 (pt) um método para renovar uma planta de amônia
BR112012024715A2 (pt) instalação de tratamento com gás quente destilado do carvão e instalação de tratamento a gás quente do forno de coque
EA201691366A1 (ru) Способ нагревания сырой нефти
EA201790647A1 (ru) Способ теплообмена для регенерации адсорбера
PH12016500893A1 (en) Method and device for steam reforming and for steam cracking of hydrocarbons
JP2017503739A5 (ru)
DOP2016000189A (es) Planta y método de purificación de fluidos por destilación
BR112017024240A2 (pt) método para tratar gás de síntese, sistema de resfriamento para resfriar gás de síntese, e sistema de gaseificação para produção de gás de síntese
PH12018501212A1 (en) Heat exchanger support structure
EA202090646A1 (ru) Теплообменник
AR081062A1 (es) Procesamiento de gases de hidrocarburos
EA201692248A1 (ru) Способы, системы и устройства для усовершенствования процессов повышения каталитической активности по фишеру-тропшу
EA201790608A1 (ru) Устройство и способ охлаждения текучей среды
PL407407A1 (pl) Instalacja odzysku ciepła z procesu toryfikacji biomasy bazująca na wymiennikach ciepła typu rurka ciepła