NO20045372L - Flertrinnshydroavsvovling av krakkete naftastrommer med en stablet sjiktreaktor - Google Patents

Flertrinnshydroavsvovling av krakkete naftastrommer med en stablet sjiktreaktor

Info

Publication number
NO20045372L
NO20045372L NO20045372A NO20045372A NO20045372L NO 20045372 L NO20045372 L NO 20045372L NO 20045372 A NO20045372 A NO 20045372A NO 20045372 A NO20045372 A NO 20045372A NO 20045372 L NO20045372 L NO 20045372L
Authority
NO
Norway
Prior art keywords
hydrodesulphurisation
multistage
bed reactor
cracked naphtha
hydrodesulfurization catalyst
Prior art date
Application number
NO20045372A
Other languages
English (en)
Inventor
Garland Barry Brignac
Bruce Randall Cook
Gary Brice Mcvicker
Richard Alan Demmin
Edward Stanley Ellis
John Peter Greeley
Thomas R Halbert
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 NO20045372L publication Critical patent/NO20045372L/no

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/19Catalysts containing parts with different compositions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/02Boron or aluminium; Oxides or hydroxides thereof
    • B01J21/04Alumina
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85Chromium, molybdenum or tungsten
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85Chromium, molybdenum or tungsten
    • B01J23/88Molybdenum
    • B01J23/882Molybdenum and cobalt
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64Pore diameter
    • B01J35/6472-50 nm
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/02Gasoline

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Fremgangsmåte for selektiv hydroavsvovling av naftastrømmer irmeholdende en vesentlig mengde olefiner og organisk bimdet svovel. Naftastrømmen er selektivt hydroavsvovlet ved å føre den gjermom en første reaksjonssone irmeholdende et sjikt med en første hydroavsvovlingskatalysator, og deretter føre den resulterende produktstrømmen gjermom en andre reaksjonssone irmeholdende et sjikt med en andre hydroavsvovlingskatalysator, der den andre hydroavsvovlingskatalysatoren irmeholder et lavere nivå katalytiske metaller erm den første hydroavsvovlingskatalysatoren.
NO20045372A 2002-05-21 2004-12-08 Flertrinnshydroavsvovling av krakkete naftastrommer med en stablet sjiktreaktor NO20045372L (no)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US38227102P 2002-05-21 2002-05-21
US10/424,332 US7297251B2 (en) 2002-05-21 2003-04-28 Multi-stage hydrodesulfurization of cracked naphtha streams with a stacked bed reactor
PCT/US2003/014705 WO2003099963A1 (en) 2002-05-21 2003-05-09 Multi-stage hydrodesulfurization of cracked naphtha streams with a stacked bed reactor

Publications (1)

Publication Number Publication Date
NO20045372L true NO20045372L (no) 2004-12-08

Family

ID=29586952

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20045372A NO20045372L (no) 2002-05-21 2004-12-08 Flertrinnshydroavsvovling av krakkete naftastrommer med en stablet sjiktreaktor

Country Status (8)

Country Link
US (1) US7297251B2 (no)
EP (1) EP1506270B1 (no)
JP (1) JP4590259B2 (no)
AU (1) AU2003241412B2 (no)
CA (1) CA2486670C (no)
ES (1) ES2642783T3 (no)
NO (1) NO20045372L (no)
WO (1) WO2003099963A1 (no)

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FR2872516B1 (fr) 2004-07-01 2007-03-09 Inst Francais Du Petrole Procede d'hydrodesulfuration des essences mettant en oeuvre un catalyseur a porosite controlee
FR2885137B1 (fr) * 2005-04-28 2007-07-13 Inst Francais Du Petrole Procede de desulfuration d'essences olefiniques
BRPI0502040A (pt) * 2005-05-13 2007-01-09 Petroleo Brasileiro Sa processo de hidrodessulfurização seletiva de nafta
US20070114156A1 (en) * 2005-11-23 2007-05-24 Greeley John P Selective naphtha hydrodesulfurization with high temperature mercaptan decomposition
BRPI0601787B1 (pt) 2006-05-17 2016-06-07 Petroleo Brasileiro Sa processo de hidrodessulfurização seletiva de nafta
US7837861B2 (en) 2006-10-18 2010-11-23 Exxonmobil Research & Engineering Co. Process for benzene reduction and sulfur removal from FCC naphthas
AR066682A1 (es) * 2007-05-25 2009-09-02 Shell Int Research Un proceso para remover azufre a partir de sendas corrientes de gas de combustible, menos reactivas y mas reactivas que contienen azufre organico y olefinas livianas
AR066681A1 (es) * 2007-05-25 2009-09-02 Shell Int Research Un proceso para remover azufre de una corriente de gas combustible
AR066680A1 (es) * 2007-05-25 2009-09-02 Shell Int Research Un proceso para remover azufre de una corriente de gas combustible, que tambien contiene dioxido de carbono y olefinas livianas
US7749375B2 (en) * 2007-09-07 2010-07-06 Uop Llc Hydrodesulfurization process
JP5123635B2 (ja) * 2007-10-12 2013-01-23 Jx日鉱日石エネルギー株式会社 ガソリン基材の製造方法及びガソリン
CN102625605A (zh) * 2011-01-27 2012-08-01 鸿富锦精密工业(深圳)有限公司 电子装置及其使用的弹开机构
US8894844B2 (en) * 2011-03-21 2014-11-25 Exxonmobil Research And Engineering Company Hydroprocessing methods utilizing carbon oxide-tolerant catalysts
US9666848B2 (en) 2011-05-20 2017-05-30 Dreamweaver International, Inc. Single-layer lithium ion battery separator
US10700326B2 (en) 2012-11-14 2020-06-30 Dreamweaver International, Inc. Single-layer lithium ion battery separators exhibiting low shrinkage rates at high temperatures
US10607790B2 (en) 2013-03-15 2020-03-31 Dreamweaver International, Inc. Direct electrolyte gelling via battery separator composition and structure
US10202553B2 (en) * 2013-10-11 2019-02-12 Cosmo Oil Co., Ltd. Hydroprocessing catalyst for heavy hydrocarbon oil, method for manufacturing hydroprocessing catalyst for heavy hydrocarbon oil, and hydroprocessing method for heavy hydrocarbon oil
US9891011B2 (en) * 2014-03-27 2018-02-13 Uop Llc Post treat reactor inlet temperature control process and temperature control device
US9850435B2 (en) 2014-08-26 2017-12-26 Exxonmobil Research And Engineering Company Hydroprocessing with drum blanketing gas compositional control
EP3585866A1 (en) 2017-02-21 2020-01-01 ExxonMobil Research and Engineering Company Desulfurization of a naphtha boiling range feed
FR3130835A1 (fr) 2021-12-20 2023-06-23 IFP Energies Nouvelles Procédé de traitement d'une essence contenant des composés soufrés comprenant une étape de dilution

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5850674B2 (ja) * 1979-05-22 1983-11-11 千代田化工建設株式会社 金属類を含有する重質油の水素化処理方法
FR2476118B1 (fr) 1980-02-19 1987-03-20 Inst Francais Du Petrole Procede de desulfuration d'un effluent de craquage catalytique ou de craquage a la vapeur
CA1182769A (en) 1980-04-10 1985-02-19 Ronald S. Tolberg Two-bed catalytic hydroprocessing for heavy hydrocarbon feedstocks
US4902404A (en) 1988-07-05 1990-02-20 Exxon Research And Engineering Company Hydrotreating process with catalyst staging
US4950383A (en) * 1989-12-08 1990-08-21 The United States Of America As Represented By The Secretary Of The Air Force Process for upgrading shale oil
US6231754B1 (en) 1996-02-02 2001-05-15 Exxon Research And Engineering Company High temperature naphtha desulfurization using a low metal and partially deactivated catalyst
US6013598A (en) 1996-02-02 2000-01-11 Exxon Research And Engineering Co. Selective hydrodesulfurization catalyst
US6126814A (en) 1996-02-02 2000-10-03 Exxon Research And Engineering Co Selective hydrodesulfurization process (HEN-9601)
US5985136A (en) 1998-06-18 1999-11-16 Exxon Research And Engineering Co. Two stage hydrodesulfurization process

Also Published As

Publication number Publication date
AU2003241412A1 (en) 2003-12-12
WO2003099963A1 (en) 2003-12-04
CA2486670C (en) 2011-04-19
US7297251B2 (en) 2007-11-20
JP4590259B2 (ja) 2010-12-01
ES2642783T3 (es) 2017-11-20
EP1506270A1 (en) 2005-02-16
CA2486670A1 (en) 2003-12-04
US20040026298A1 (en) 2004-02-12
EP1506270B1 (en) 2017-08-02
JP2006508196A (ja) 2006-03-09
AU2003241412B2 (en) 2008-11-20

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