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DE68921025D1 - Hydrierungskatalysator, seine Herstellung und seine Verwendung. - Google Patents

Hydrierungskatalysator, seine Herstellung und seine Verwendung.

Info

Publication number
DE68921025D1
DE68921025D1 DE68921025T DE68921025T DE68921025D1 DE 68921025 D1 DE68921025 D1 DE 68921025D1 DE 68921025 T DE68921025 T DE 68921025T DE 68921025 T DE68921025 T DE 68921025T DE 68921025 D1 DE68921025 D1 DE 68921025D1
Authority
DE
Germany
Prior art keywords
manufacture
hydrogenation catalyst
hydrogenation
catalyst
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 - Fee Related
Application number
DE68921025T
Other languages
English (en)
Other versions
DE68921025T2 (de
Inventor
Howard D Simpson
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.)
Union Oil Company of California
Original Assignee
Union Oil Company of California
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 Union Oil Company of California filed Critical Union Oil Company of California
Application granted granted Critical
Publication of DE68921025D1 publication Critical patent/DE68921025D1/de
Publication of DE68921025T2 publication Critical patent/DE68921025T2/de
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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
    • 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
    • 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
    • B01J23/883Molybdenum and nickel
    • 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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02Refining 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
    • C10G45/04Refining 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
    • 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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02Refining 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
    • C10G45/04Refining 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
    • C10G45/06Refining 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
    • C10G45/08Refining 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
    • 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
    • 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
    • B01J35/66Pore distribution
    • 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
    • B01J35/66Pore distribution
    • B01J35/67Pore distribution monomodal

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
DE68921025T 1988-06-29 1989-06-23 Hydrierungskatalysator, seine Herstellung und seine Verwendung. Expired - Fee Related DE68921025T2 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US07/213,079 US4886582A (en) 1988-06-29 1988-06-29 Resid hydroprocessing catalyst and method of preparation

Publications (2)

Publication Number Publication Date
DE68921025D1 true DE68921025D1 (de) 1995-03-23
DE68921025T2 DE68921025T2 (de) 1995-06-01

Family

ID=22793662

Family Applications (1)

Application Number Title Priority Date Filing Date
DE68921025T Expired - Fee Related DE68921025T2 (de) 1988-06-29 1989-06-23 Hydrierungskatalysator, seine Herstellung und seine Verwendung.

Country Status (4)

Country Link
US (1) US4886582A (de)
EP (1) EP0349223B1 (de)
JP (1) JPH0263553A (de)
DE (1) DE68921025T2 (de)

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5338717A (en) * 1990-12-24 1994-08-16 Exxon Research And Engineering Company Method for the preparation of supported hydrogenation and hydrotreating catalysts
CA2056511C (en) * 1990-12-24 1999-06-01 Clyde Lee Aldridge Supported hydrogenation and hydrotreating catalysts and process
US5336654A (en) * 1990-12-24 1994-08-09 Exxon Research And Engineering Company Method for the preparation of supported hydrogenation and hydrotreating catalysts
JP3416177B2 (ja) * 1991-10-02 2003-06-16 シェブロン リサーチ アンド テクノロジー カンパニー 高活性残油触媒の製造方法
US5320743A (en) * 1992-05-29 1994-06-14 Texaco Inc. Mild hydrocracking of heavy hydrocarbon feedstocks employing silica-alumina catalysts
US5332709A (en) * 1993-03-22 1994-07-26 Om Group, Inc. (Mooney Chemicals, Inc.) Stabilized aqueous solutions for preparing catalysts and process for preparing catalysts
DE4310971A1 (de) * 1993-04-03 1994-10-06 Huels Chemische Werke Ag Nickel/Aluminiumoxid-Katalysator, Verfahren zu seiner Herstellung, seine Verwendung sowie Verfahren zur Hydrierung von aromatischen Kohlenwasserstoffen mit Hilfe des Katalysators
US5710088A (en) * 1995-06-30 1998-01-20 Ford Global Technologies, Inc. Lean-NOx catalysts containing silver supported on alumina
DE19533486A1 (de) * 1995-09-12 1997-03-13 Basf Ag Monomodale und polymodale Katalysatorträger und Katalysatoren mit engen Porengrößenverteilungen und deren Herstellverfahren
DE19533484A1 (de) * 1995-09-12 1997-03-13 Basf Ag Monomodale und polymodale Katalysatorträger und Katalysatoren mit engen Porengrößenverteilungen und deren Herstellverfahren
JP3955096B2 (ja) * 1996-02-02 2007-08-08 エクソンモービル リサーチ アンド エンジニアリング カンパニー 選択的水素化脱硫触媒及び方法
US6013598A (en) * 1996-02-02 2000-01-11 Exxon Research And Engineering Co. Selective hydrodesulfurization catalyst
EP1273336B1 (de) * 1998-12-25 2008-01-23 Tosoh Corporation Verfahren zur Entfernung von organischen Verbindungen mittels Verbrennungskatalysatoren
US6870014B2 (en) * 2000-07-03 2005-03-22 Basf Aktiengesellschaft Catalyst and method for producing polytetrahydrofurane
JP3881162B2 (ja) * 2000-07-12 2007-02-14 触媒化成工業株式会社 水素化処理成形触媒およびその製造方法
JP4612229B2 (ja) * 2001-06-08 2011-01-12 日本ケッチェン株式会社 重質炭化水素油の水素化処理用触媒並びに水素化処理方法
JP2003181292A (ja) * 2002-12-25 2003-07-02 Chevron Research & Technology Co 高活性残油触媒
CN102698769B (zh) * 2006-08-03 2016-08-24 国际壳牌研究有限公司 含有钼和第viii族金属的催化剂及其用于加氢脱硫氢馏分油的用途
US20100240522A1 (en) 2009-03-23 2010-09-23 Tomoyuki Inui Catalyst exhibiting hydrogen spillover effect
US11084023B2 (en) * 2019-03-22 2021-08-10 Purdue Research Foundation Phosphate-promoted nickel catalyst for high temperature oligomerization

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3242101A (en) * 1962-07-24 1966-03-22 Sinclair Research Inc Nickel-molybdenum-alumina hydrocarbon conversion catalyst
US4113661A (en) * 1973-08-09 1978-09-12 Chevron Research Company Method for preparing a hydrodesulfurization catalyst
US3980552A (en) * 1975-05-05 1976-09-14 Union Oil Company Of California Hydrodesulfurization of residual petroleum oil with a sulfided cobalt-molybdenum-alumina catalyst
US4069139A (en) * 1975-12-29 1978-01-17 Exxon Research & Engineering Co. Hydrodesulfurization of oil utilizing a narrow pore size distribution 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
US4306965A (en) * 1979-03-19 1981-12-22 Standard Oil Company (Indiana) Hydrotreating process
US4224144A (en) * 1979-03-19 1980-09-23 Standard Oil Company (Indiana) Hydrotreating a hydrocarbon stream to remove nitrogen and sulfur
CA1161326A (en) * 1979-09-10 1984-01-31 Robert F. Shaw Abherent surgical instrument and method
JPS56133035A (en) * 1980-03-25 1981-10-17 Shokubai Kasei Kogyo Kk Catalyst composition for hydrogenolysis
US4500424A (en) * 1983-04-07 1985-02-19 Union Oil Company Of California Desulfurization catalyst and process
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
JPS62199687A (ja) * 1986-04-28 1987-09-03 ユニオン・オイル・コンパニ−・オブ・カリフオルニア 細孔の大きい触媒を用いる水素化法
US4738944A (en) * 1986-12-05 1988-04-19 Union Oil Company Of California Ni-P-Mo catalyst and hydroprocessing use thereof

Also Published As

Publication number Publication date
EP0349223A1 (de) 1990-01-03
JPH0263553A (ja) 1990-03-02
EP0349223B1 (de) 1995-02-08
US4886582A (en) 1989-12-12
DE68921025T2 (de) 1995-06-01

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Legal Events

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8364 No opposition during term of opposition
8339 Ceased/non-payment of the annual fee