JPH0554385B2 - - Google Patents

Info

Publication number
JPH0554385B2
JPH0554385B2 JP8675385A JP7538586A JPH0554385B2 JP H0554385 B2 JPH0554385 B2 JP H0554385B2 JP 8675385 A JP8675385 A JP 8675385A JP 7538586 A JP7538586 A JP 7538586A JP H0554385 B2 JPH0554385 B2 JP H0554385B2
Authority
JP
Japan
Prior art keywords
catalyst
group
periodic table
alumina support
pore volume
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Lifetime
Application number
JP8675385A
Other languages
English (en)
Japanese (ja)
Other versions
JPS62232488A (ja
Inventor
Ruisu Morarusu Arufuretsudo
Ii Gariaso Robaato
Magudarena Agudero Maria
Arumando Sarazaaru Jose
Rafuaeru Karasukueru Enjeru
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Petroleos de Venezuela SA
Original Assignee
Petroleos de Venezuela SA
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 Petroleos de Venezuela SA filed Critical Petroleos de Venezuela SA
Publication of JPS62232488A publication Critical patent/JPS62232488A/ja
Publication of JPH0554385B2 publication Critical patent/JPH0554385B2/ja
Granted legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14—Phosphorus; Compounds thereof
    • B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C10G45/08—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
JP61075385A 1983-12-19 1986-04-01 重質原油の水素化処理用触媒，その製法，および水素化処理方法 Granted JPS62232488A (ja)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US06/563,197 US4520128A (en) 1983-12-19 1983-12-19 Catalyst having high metal retention capacity and good stability for use in the demetallization of heavy crudes and method of preparation of same

Publications (2)

Publication Number Publication Date
JPS62232488A JPS62232488A (ja) 1987-10-12
JPH0554385B2 true JPH0554385B2 (en, 2012) 1993-08-12

Family

ID=24249509

Family Applications (2)

Application Number Title Priority Date Filing Date
JP60203222A Pending JPS6265750A (ja) 1983-12-19 1985-09-13 重油等の水素化処理用触媒及びその製造方法
JP61075385A Granted JPS62232488A (ja) 1983-12-19 1986-04-01 重質原油の水素化処理用触媒，その製法，および水素化処理方法

Family Applications Before (1)

Application Number Title Priority Date Filing Date
JP60203222A Pending JPS6265750A (ja) 1983-12-19 1985-09-13 重油等の水素化処理用触媒及びその製造方法

Country Status (5)

Country Link
US (1) US4520128A (en, 2012)
JP (2) JPS6265750A (en, 2012)
DE (1) DE3446038A1 (en, 2012)
FR (1) FR2556611B1 (en, 2012)
GB (4) GB2151499B (en, 2012)

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US4600703A (en) * 1983-12-19 1986-07-15 Intevep, S.A. Catalyst for the hydrocracking of heavy vacuum gas oils, method of preparation of catalyst and process for use thereof in the mild hydrocracking of heavy vacuum gas oils
US4579649A (en) * 1983-12-19 1986-04-01 Intevep, S.A. Process for demetallization of heavy crudes using a catalyst having high metal retention capacity and good stability
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US5827421A (en) * 1992-04-20 1998-10-27 Texaco Inc Hydroconversion process employing catalyst with specified pore size distribution and no added silica
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US5320743A (en) * 1992-05-29 1994-06-14 Texaco Inc. Mild hydrocracking of heavy hydrocarbon feedstocks employing silica-alumina catalysts
US5358629A (en) * 1993-01-21 1994-10-25 Texaco Inc. Hydroconversion process containing a molybdenum complex recovered from epoxidation of olefinic hydrocarbons
US5397456A (en) * 1993-02-19 1995-03-14 Texaco Inc. Hydroconversion process employing catalyst with specified pore size distribution
US6093309A (en) * 1993-05-04 2000-07-25 Cri International, Inc. Method of treating spontaneously combustible catalysts
ZA942966B (en) * 1993-05-04 1995-01-19 Cri Int Inc A method of treating spontaneously combustible catalysts.
US5389595A (en) * 1993-09-30 1995-02-14 Union Oil Company Of California Hydroprocessing catalyst, its use, and method of preparation
JP3821483B2 (ja) * 1993-09-30 2006-09-13 ユーオーピー 水素化処理用の触媒とその利用法
US5928499A (en) * 1993-10-01 1999-07-27 Texaco Inc Hydroconversion process employing catalyst with specified pore size distribution, median pore diameter by surface area, and pore mode by volume
US5514273A (en) * 1993-10-01 1996-05-07 Texaco Inc. Hydroconversion process employing catalyst with specified pore size distribution
US5968348A (en) * 1994-05-16 1999-10-19 Texaco Inc. Hydroconversion process employing a phosphorus loaded NiMo catalyst with specified pore size distribution
AU2614095A (en) * 1994-05-16 1995-12-05 Shell Internationale Research Maatschappij B.V. Process for upgrading residual hydrocarbon oils
US5821191A (en) * 1996-06-17 1998-10-13 Shell Oil Company Process for presulfiding hydrocarbon processing catalysts
US5786293A (en) * 1996-06-17 1998-07-28 Shell Oil Company Process for presulfiding hydrocarbon processing catalysts
JP4538014B2 (ja) * 1998-12-08 2010-09-08 株式会社ジャパンエナジー 水素化精製用触媒
EP1240276A4 (en) 1999-09-30 2003-07-02 Shigeo T Oyama INNOVATIVE TRANSITION METAL PHOSPHIDE CATALYST
FR2839902B1 (fr) * 2002-05-24 2007-06-29 Inst Francais Du Petrole Catalyseur d'hydroraffinage et/ou d'hydroconversion et son utilisation dans des procedes d'hydrotraitement de charges hydrocarbonees
US7390766B1 (en) * 2003-11-20 2008-06-24 Klein Darryl P Hydroconversion catalysts and methods of making and using same
US20050109674A1 (en) * 2003-11-20 2005-05-26 Advanced Refining Technologies Llc Hydroconversion catalysts and methods of making and using same
JP4493997B2 (ja) * 2003-12-10 2010-06-30 財団法人石油産業活性化センター 炭化水素油の水素化脱硫触媒及びその製造方法
US8608946B2 (en) * 2003-12-19 2013-12-17 Shell Oil Company Systems, methods, and catalysts for producing a crude product
US20070000808A1 (en) * 2003-12-19 2007-01-04 Bhan Opinder K Method and catalyst for producing a crude product having selected properties
US20070000810A1 (en) * 2003-12-19 2007-01-04 Bhan Opinder K Method for producing a crude product with reduced tan
BRPI0405720B1 (pt) * 2003-12-19 2014-03-04 Shell Int Research Métodos de produzir um produto de petróleo bruto e combustível de transporte, combustível de aquecimento, lubrificante ou substâncias químicas, produto de petróleo bruto e sistema para produzir um produto de petróleo bruto
US20100098602A1 (en) * 2003-12-19 2010-04-22 Opinder Kishan Bhan Systems, methods, and catalysts for producing a crude product
US7745369B2 (en) * 2003-12-19 2010-06-29 Shell Oil Company Method and catalyst for producing a crude product with minimal hydrogen uptake
TWI415930B (zh) * 2005-04-06 2013-11-21 Shell Int Research 減少液態含烴原料總酸值（ｔａｎ）的方法
BRPI0610669A2 (pt) * 2005-04-11 2017-01-31 Shell Int Research método para produzir um produto bruto
WO2006110546A2 (en) * 2005-04-11 2006-10-19 Shell Internationale Research Maatschappij B.V. Systems, methods, and catalysts for producing a crude product
CA2604012C (en) * 2005-04-11 2013-11-19 Shell Internationale Research Maatschappij B.V. Method and catalyst for producing a crude product having a reduced mcr content
RU2007141712A (ru) * 2005-04-11 2009-05-20 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL) Способ получения полупродукта с пониженным содержанием азота и катализатор для его осуществления
WO2007149923A2 (en) * 2006-06-22 2007-12-27 Shell Oil Company Method for producing a crude product with a long-life catalyst
US20080087578A1 (en) * 2006-10-06 2008-04-17 Bhan Opinder K Methods for producing a crude product and compositions thereof
KR100885310B1 (ko) * 2007-07-26 2009-02-24 한국화학연구원 피셔-트롭쉬 합성용 코발트／인―알루미나 촉매와 이의제조방법
EP2321046A4 (en) * 2008-04-10 2013-12-18 Shell Int Research CATALYSIS SYSTEMS AND METHODS FOR CONVERTING RAW FOOD USING SUCH CATALYSIS SYSTEMS
MX2009002359A (es) * 2009-03-03 2010-10-01 Mexicano Inst Petrol Catalizador soportado en carbon para la desmetalizacion de crudos pesados y residuos.
US20100240522A1 (en) 2009-03-23 2010-09-23 Tomoyuki Inui Catalyst exhibiting hydrogen spillover effect
US20130105357A1 (en) * 2011-10-27 2013-05-02 Shell Oil Company Self-activating hydroprocessing catalyst and process for treating heavy hydrocarbon feedstocks
US20150119233A1 (en) * 2013-10-30 2015-04-30 Basf Corporation Highly dispersed metal oxide catalyst coatings
CN111318294A (zh) * 2018-12-13 2020-06-23 中国石油化工股份有限公司 一种加氢处理催化剂及其制备方法和应用

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Also Published As

Publication number Publication date
GB2191957B (en) 1988-10-26
FR2556611B1 (fr) 1993-04-30
GB8510358D0 (en) 1985-05-30
FR2556611A1 (fr) 1985-06-21
GB2151499A (en) 1985-07-24
JPS62232488A (ja) 1987-10-12
GB2174015A (en) 1986-10-29
DE3446038A1 (de) 1985-06-27
GB2156847A (en) 1985-10-16
GB2151499B (en) 1988-10-26
GB8510359D0 (en) 1985-05-30
GB2191957A (en) 1987-12-31
GB8710349D0 (en) 1987-06-03
JPS6265750A (ja) 1987-03-25
DE3446038C2 (en, 2012) 1993-02-18
US4520128A (en) 1985-05-28
GB2156847B (en) 1988-12-14
GB8431941D0 (en) 1985-01-30

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EXPY Cancellation because of completion of term