ATE69255T1 - Katalysatoren fuer die hydrierende umwandlung von schweroelen. - Google Patents

Katalysatoren fuer die hydrierende umwandlung von schweroelen.

Info

Publication number
ATE69255T1
ATE69255T1 AT86105476T AT86105476T ATE69255T1 AT E69255 T1 ATE69255 T1 AT E69255T1 AT 86105476 T AT86105476 T AT 86105476T AT 86105476 T AT86105476 T AT 86105476T AT E69255 T1 ATE69255 T1 AT E69255T1
Authority
AT
Austria
Prior art keywords
catalysts
heavy oils
hydrogenic
conversion
cobalt
Prior art date
Application number
AT86105476T
Other languages
English (en)
Inventor
John Francis Lindsley
Marvin Goldstein
William Harold Quayle
Original Assignee
American Cyanamid 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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=24936074&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=ATE69255(T1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by American Cyanamid Co filed Critical American Cyanamid Co
Application granted granted Critical
Publication of ATE69255T1 publication Critical patent/ATE69255T1/de

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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/66—Pore distribution
    • 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
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/12—Silica and alumina
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76—Catalysts 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
    • B01J23/84—Catalysts 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
    • B01J23/85—Chromium, molybdenum or tungsten
    • B01J23/88—Molybdenum
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76—Catalysts 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
    • B01J23/84—Catalysts 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
    • B01J23/85—Chromium, molybdenum or tungsten
    • B01J23/88—Molybdenum
    • B01J23/883—Molybdenum and nickel
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64—Pore diameter
    • B01J35/647—2-50 nm
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64—Pore diameter
    • B01J35/651—50-500 nm
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/08—Heat treatment
    • B01J37/10—Heat treatment in the presence of water, e.g. steam
    • 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)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
AT86105476T 1985-05-06 1986-04-21 Katalysatoren fuer die hydrierende umwandlung von schweroelen. ATE69255T1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US06/730,619 US4652545A (en) 1985-05-06 1985-05-06 Catalyst for hydroconversion of heavy oils and method of making the catalyst
EP86105476A EP0201762B2 (de) 1985-05-06 1986-04-21 Katalysatoren für die hydrierende Umwandlung von Schwerölen

Publications (1)

Publication Number Publication Date
ATE69255T1 true ATE69255T1 (de) 1991-11-15

Family

ID=24936074

Family Applications (1)

Application Number Title Priority Date Filing Date
AT86105476T ATE69255T1 (de) 1985-05-06 1986-04-21 Katalysatoren fuer die hydrierende umwandlung von schweroelen.

Country Status (7)

Country Link
US (1) US4652545A (de)
EP (1) EP0201762B2 (de)
JP (1) JP2537193B2 (de)
AT (1) ATE69255T1 (de)
CA (1) CA1264726A (de)
DE (1) DE3682319D1 (de)
MX (1) MX163973B (de)

Families Citing this family (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4786403A (en) * 1986-10-28 1988-11-22 Shell Oil Company Process for hydrotreating hydro carbon feeds
US4786404A (en) * 1986-10-28 1988-11-22 Shell Oil Company Process for hydrotreating hydrocarbon feeds
US4941964A (en) * 1988-03-14 1990-07-17 Texaco Inc. Hydrotreatment process employing catalyst with specified pore size distribution
US5047142A (en) * 1988-05-13 1991-09-10 Texaco Inc. Catalyst composition and method for hydroprocessing petroleum feedstocks
US4969990A (en) * 1988-06-29 1990-11-13 Union Oil Company Of California Hydroprocessing with a catalyst having a narrow pore size distribution
US5868923A (en) * 1991-05-02 1999-02-09 Texaco Inc Hydroconversion process
EP0526988A3 (en) * 1991-07-10 1993-03-31 Texaco Development Corporation Hydrotreatment process employing a mono-modal catalyst with specified pore size distribution
US5210061A (en) * 1991-09-24 1993-05-11 Union Oil Company Of California Resid hydroprocessing catalyst
US5192734A (en) * 1991-10-25 1993-03-09 W. R. Grace & Co.- Conn. Hydroprocessing catalyst composition
US5322616A (en) * 1992-03-30 1994-06-21 Texaco Inc. Mild hydrocracking of heavy hydrocarbon feedstocks employing lithia promoted catalysts
US5320743A (en) * 1992-05-29 1994-06-14 Texaco Inc. Mild hydrocracking of heavy hydrocarbon feedstocks employing silica-alumina catalysts
US5397456A (en) * 1993-02-19 1995-03-14 Texaco Inc. Hydroconversion process employing catalyst with specified pore size distribution
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
US6015485A (en) * 1994-05-13 2000-01-18 Cytec Technology Corporation High activity catalysts having a bimodal mesopore structure
US5968348A (en) * 1994-05-16 1999-10-19 Texaco Inc. Hydroconversion process employing a phosphorus loaded NiMo catalyst with specified pore size distribution
US6387248B2 (en) 1997-11-06 2002-05-14 Texaco Inc. Method of preparing a catalyst for use in the hydrotreating of high boiling hydrocarbon feedstocks
GC0000065A (en) * 1998-09-01 2004-06-30 Japan Energy Corp Hydrocracking catalyst, producing method threof, and hydrocracking method.
US6508999B1 (en) * 2000-11-21 2003-01-21 Shell Oil Company Aluminum trihydroxide phase
US6589908B1 (en) 2000-11-28 2003-07-08 Shell Oil Company Method of making alumina having bimodal pore structure, and catalysts made therefrom
EP1552880B1 (de) * 2002-10-10 2014-07-02 China Petroleum & Chemical Corporation Siliciumhaltiger aluminiumoxidträger, dessen herstellung und ein katalysator, der den aluminiumoxidträger enthält
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
US20100240522A1 (en) 2009-03-23 2010-09-23 Tomoyuki Inui Catalyst exhibiting hydrogen spillover effect
US10400184B2 (en) * 2011-08-31 2019-09-03 Exxonmobil Research And Engineering Company Hydroprocessing of heavy hydrocarbon feeds using small pore catalysts
JP6134334B2 (ja) 2011-12-22 2017-05-24 アドバンスド・リフアイニング・テクノロジーズ・エルエルシー シリカ含有アルミナ担体、それから生じさせた触媒およびそれの使用方法
MX345342B (es) 2012-08-20 2017-01-24 Inst Mexicano Del Petróleo Procedimiento para el mejoramiento de crudos pesados y extrapesados.
US10537883B2 (en) 2016-10-07 2020-01-21 King Fahd University Of Petroleum And Minerals Method for producing a hydrodesulfurization catalyst

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3383301A (en) * 1966-01-20 1968-05-14 Gulf Research Development Co Residue desulfurization with catalyst whose pore volume is distributed over wide range of pore sizes
US3509044A (en) * 1967-06-26 1970-04-28 Exxon Research Engineering Co Hydrodesulfurization of petroleum residuum
US4113661A (en) * 1973-08-09 1978-09-12 Chevron Research Company Method for preparing a hydrodesulfurization catalyst
US4048060A (en) * 1975-12-29 1977-09-13 Exxon Research And Engineering Company Two-stage hydrodesulfurization of oil utilizing a narrow pore size distribution catalyst
US4069139A (en) * 1975-12-29 1978-01-17 Exxon Research & Engineering Co. Hydrodesulfurization of oil utilizing a narrow pore size distribution catalyst
US4013547A (en) * 1976-01-22 1977-03-22 Union Oil Company Of California Desulfurization of residual petroleum oils with a catalyst calcined at higher temperatures
US4051021A (en) * 1976-05-12 1977-09-27 Exxon Research & Engineering Co. Hydrodesulfurization of hydrocarbon feed utilizing a silica stabilized alumina composite catalyst
JPS5527036A (en) * 1978-08-16 1980-02-26 Shokubai Kasei Kogyo Kk Hydrogenation and desulfurization catalyst for heavy hydrocabron oil
JPS55119445A (en) * 1979-03-07 1980-09-13 Shokubai Kasei Kogyo Kk Desulfurization catalyst of petroleum base heavy hydrocarbon oil
US4414141A (en) * 1980-11-21 1983-11-08 The Lummus Company Hydrotreating catalyst
JPS594440A (ja) * 1982-06-29 1984-01-11 Shokubai Kasei Kogyo Kk 水素化精製触媒の製造法
JPS59115743A (ja) * 1982-12-23 1984-07-04 Res Assoc Petroleum Alternat Dev<Rapad> 重質炭化水素油の水素化処理触媒用担体
US4500424A (en) * 1983-04-07 1985-02-19 Union Oil Company Of California Desulfurization catalyst and process

Also Published As

Publication number Publication date
MX163973B (es) 1992-07-07
EP0201762A2 (de) 1986-11-20
CA1264726A (en) 1990-01-23
EP0201762B1 (de) 1991-11-06
JPS61287448A (ja) 1986-12-17
EP0201762B2 (de) 1997-04-02
JP2537193B2 (ja) 1996-09-25
US4652545A (en) 1987-03-24
DE3682319D1 (de) 1991-12-12
EP0201762A3 (en) 1988-06-01

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