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NO20062864L - Fremgangsmate og apparat for a separere aromatiske hydrokarboner i et ikke-adiabatisk membransystem - Google Patents

Fremgangsmate og apparat for a separere aromatiske hydrokarboner i et ikke-adiabatisk membransystem

Info

Publication number
NO20062864L
NO20062864L NO20062864A NO20062864A NO20062864L NO 20062864 L NO20062864 L NO 20062864L NO 20062864 A NO20062864 A NO 20062864A NO 20062864 A NO20062864 A NO 20062864A NO 20062864 L NO20062864 L NO 20062864L
Authority
NO
Norway
Prior art keywords
feed stream
aromatic hydrocarbons
separating
membrane system
permeate
Prior art date
Application number
NO20062864A
Other languages
English (en)
Inventor
John G Matragrano
Craig Y Sabottke
Original Assignee
Exxonmobil Res & Eng 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 Res & Eng Co filed Critical Exxonmobil Res & Eng Co
Publication of NO20062864L publication Critical patent/NO20062864L/no

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/24—Dialysis ; Membrane extraction
    • B01D61/28—Apparatus therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/36—Pervaporation; Membrane distillation; Liquid permeation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/08—Flat membrane modules
    • B01D63/082—Flat membrane modules comprising a stack of flat membranes
    • B01D63/0822—Plate-and-frame devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/08—Flat membrane modules
    • B01D63/082—Flat membrane modules comprising a stack of flat membranes
    • B01D63/084—Flat membrane modules comprising a stack of flat membranes at least one flow duct intersecting the membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/10—Supported membranes; Membrane supports
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
    • C10G31/11—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by dialysis
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2313/00—Details relating to membrane modules or apparatus
    • B01D2313/20—Specific housing
    • B01D2313/201—Closed housing, vessels or containers
    • B01D2313/2011—Pressure vessels
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2313/00—Details relating to membrane modules or apparatus
    • B01D2313/22—Cooling or heating elements

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Urology & Nephrology (AREA)
  • Health & Medical Sciences (AREA)
  • Organic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

En isotermisk fremgangsmåte er tilveiebrakt for å separere aromatiske hydrokarboner fra en fødestrøm. Fremgangsmåten inkluderer å strømme fødestrømmen gjennom en første kanal innenfor en første lamellsammenstilling som inneholder et ribbeelement. Deretter blir fødestrømmen eksponert for en første tynnfilmpolymermembran. En strøm trenger gjennom den første tynnfilmpolymermembranen inn i en permeatsone. Permeatsonen varmes opp via et oppvarmet fluid som finnes innenfor ribbeelementet. Permeatet er produsert fra den første lamellsammenstillingen. Fremgangsmåten kan inkludere å ha et flertall tandemlamellsammenstillinger arrangert i rekke. En apparatur for å separere de aromatiske komponentene fra en fødestrøm er også vist. I den foretrukne utførelsen inkluderer apparaturen en rekke tandemlamellsammenstillinger spesielt tilpasset for å blande et transportdrivstoff.
NO20062864A 2003-11-18 2006-06-19 Fremgangsmate og apparat for a separere aromatiske hydrokarboner i et ikke-adiabatisk membransystem NO20062864L (no)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US52313103P 2003-11-18 2003-11-18
PCT/US2004/037332 WO2005049182A1 (en) 2003-11-18 2004-11-18 Method and apparatus for separating aromatic hydrocarbons in a non-adiabatic membrane system

Publications (1)

Publication Number Publication Date
NO20062864L true NO20062864L (no) 2006-08-18

Family

ID=34619571

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20062864A NO20062864L (no) 2003-11-18 2006-06-19 Fremgangsmate og apparat for a separere aromatiske hydrokarboner i et ikke-adiabatisk membransystem

Country Status (7)

Country Link
US (1) US7314565B2 (no)
EP (1) EP1689515A1 (no)
JP (1) JP2007511364A (no)
AU (1) AU2004291500A1 (no)
CA (1) CA2543876A1 (no)
NO (1) NO20062864L (no)
WO (1) WO2005049182A1 (no)

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US7892321B2 (en) * 2006-02-01 2011-02-22 Intelligent Energy, Inc. Integrated heated prevaporation module
CN101516808B (zh) * 2006-07-14 2013-01-23 埃克森美孚研究工程公司 使用混合蒸气-液体原料的改良膜分离方法
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US8071006B2 (en) * 2008-08-12 2011-12-06 General Electric Company Poly(tetrafluoroethylene) zeolite composite and methods
US8211300B2 (en) * 2008-12-22 2012-07-03 Exxonmobil Research And Engineering Company Vehicle-mounted fuel separation system
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US20100237013A1 (en) * 2009-02-13 2010-09-23 Millipore Corporation Autonomous filter element
WO2011002745A1 (en) * 2009-07-01 2011-01-06 Saudi Arabian Oil Company Membrane desulfurization of liquid hydrocarbons using an extractive liquid membrane contactor system and method
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TWI590372B (zh) * 2012-08-31 2017-07-01 聯達科技設備私人有限公司 用於晶圓及膜片架的單一超平坦晶圓臺結構
CN103272430A (zh) * 2013-05-14 2013-09-04 江苏国望高科纤维有限公司 一种延长功能性聚酯生产装置预聚物过滤器切换周期的方法
EP3122440B1 (en) * 2014-03-25 2018-11-21 Dow Silicones Corporation Method of separating volatile siloxane from a liquid feed mixture
US10478778B2 (en) 2015-07-01 2019-11-19 3M Innovative Properties Company Composite membranes with improved performance and/or durability and methods of use
CN107735163B (zh) 2015-07-01 2021-02-23 3M创新有限公司 含pvp和/或pvl的复合膜以及使用方法
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Also Published As

Publication number Publication date
WO2005049182A1 (en) 2005-06-02
AU2004291500A1 (en) 2005-06-02
EP1689515A1 (en) 2006-08-16
US20050103715A1 (en) 2005-05-19
CA2543876A1 (en) 2005-06-02
US7314565B2 (en) 2008-01-01
JP2007511364A (ja) 2007-05-10

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