DK171345B1 - Fremgangsmåde til fremstilling af hydrobehandlingskatalysatorer ud fra hydrogeler samt katalysatorer fremstillet ved fremgangsmåden - Google Patents

Fremgangsmåde til fremstilling af hydrobehandlingskatalysatorer ud fra hydrogeler samt katalysatorer fremstillet ved fremgangsmåden Download PDF

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Publication number
DK171345B1
DK171345B1 DK562187A DK562187A DK171345B1 DK 171345 B1 DK171345 B1 DK 171345B1 DK 562187 A DK562187 A DK 562187A DK 562187 A DK562187 A DK 562187A DK 171345 B1 DK171345 B1 DK 171345B1
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Prior art keywords
range
precipitate
temperature
nickel
salts
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DK562187A
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Danish (da)
English (en)
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DK562187A (da
DK562187D0 (da
Inventor
Richard Alan Kemp
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Shell Int Research
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Publication of DK562187A publication Critical patent/DK562187A/da
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    • 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
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14Phosphorus; Compounds thereof
    • B01J27/186Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14Phosphorus; Compounds thereof
    • B01J27/186Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • B01J27/19Molybdenum
    • 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
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/31Density
    • 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
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61Surface area
    • B01J35/615100-500 m2/g
    • 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
    • B01J35/61Surface area
    • B01J35/617500-1000 m2/g
    • 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
    • B01J35/63Pore volume
    • B01J35/6350.5-1.0 ml/g
    • 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
    • B01J35/63Pore volume
    • B01J35/638Pore volume more than 1.0 ml/g
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (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)
DK562187A 1986-10-28 1987-10-27 Fremgangsmåde til fremstilling af hydrobehandlingskatalysatorer ud fra hydrogeler samt katalysatorer fremstillet ved fremgangsmåden DK171345B1 (da)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US06/924,227 US4717707A (en) 1986-10-28 1986-10-28 Hydrotreating catalysts prepared from hydrogels
US92422786 1986-10-28

Publications (3)

Publication Number Publication Date
DK562187D0 DK562187D0 (da) 1987-10-27
DK562187A DK562187A (da) 1988-04-29
DK171345B1 true DK171345B1 (da) 1996-09-16

Family

ID=25449921

Family Applications (1)

Application Number Title Priority Date Filing Date
DK562187A DK171345B1 (da) 1986-10-28 1987-10-27 Fremgangsmåde til fremstilling af hydrobehandlingskatalysatorer ud fra hydrogeler samt katalysatorer fremstillet ved fremgangsmåden

Country Status (6)

Country Link
US (1) US4717707A (de)
EP (1) EP0266008B1 (de)
JP (1) JP2556340B2 (de)
CA (1) CA1312594C (de)
DE (1) DE3762090D1 (de)
DK (1) DK171345B1 (de)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4820679A (en) * 1987-11-20 1989-04-11 Shell Oil Company Hydrotreating catalysts prepared from hydrogels
US4880524A (en) * 1987-11-20 1989-11-14 Shell Oil Company Process for hydrotreating hydrocarbon feeds
JP3272384B2 (ja) * 1991-10-24 2002-04-08 財団法人石油産業活性化センター 触媒組成物及びその製造方法ならびに該触媒組成物を用いる含硫炭化水素の水素化脱硫方法
ES2376720T3 (es) * 1998-03-20 2012-03-16 China Petrochemical Corporation Catalizador para el hidrotratamiento de destilados de aceites ligeros y preparación del mismo.
US20050109674A1 (en) * 2003-11-20 2005-05-26 Advanced Refining Technologies Llc Hydroconversion catalysts and methods of making and using same
US7390766B1 (en) 2003-11-20 2008-06-24 Klein Darryl P Hydroconversion catalysts and methods of making and using same
RU2623432C1 (ru) * 2016-05-17 2017-06-26 Акционерное общество "Ангарский завод катализаторов и органического синтеза" (АО "АЗКиОС") Способ приготовления носителя для катализатора гидроочистки нефтяных фракций
BR102016022467B1 (pt) * 2016-09-28 2022-02-01 Petróleo Brasileiro S.A. - Petrobras Processo para preparação de um catalisador à base de níquel, catalisador à base de níquel, e, seu uso em um processo de reforma a vapor

Family Cites Families (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3124418A (en) * 1964-03-10 Nitric acid
US2441297A (en) * 1944-05-03 1948-05-11 Union Oil Co Process for dehydrogenation of hydrocarbons by contact with catalysts supported on alumina stabilized by aluminum phosphate
US3232887A (en) * 1962-05-07 1966-02-01 Nalco Chemical Co Stabilized aqueous solutions for use in impregnating catalyst carriers and method of making same
GB1076450A (en) * 1963-12-06 1967-07-19 Grace W R & Co Improvements relating to the production of alumina gels
US3493517A (en) * 1967-10-02 1970-02-03 Chevron Res Metal phosphate containing catalysts and preparation thereof
US3864461A (en) * 1972-08-29 1975-02-04 Laporte Industries Ltd Process for the production of alumina
US4019978A (en) * 1972-08-29 1977-04-26 Laporte Industries Limited Process for the production of alumina
US3879310A (en) * 1973-03-26 1975-04-22 Kaiser Aluminium Chem Corp Surface stabilized active alumina
US4202798A (en) * 1973-06-12 1980-05-13 Atlantic Richfield Company Phosphorous-containing catalyst and method for preparing and using same
US3969273A (en) * 1975-04-24 1976-07-13 W. R. Grace & Co. Process for preparing phosphated alumina extrudates
US4003828A (en) * 1975-07-23 1977-01-18 Exxon Research And Engineering Company Catalyst and process for removing sulfur and metal contaminants from hydrocarbon feedstocks
US4066572A (en) * 1976-10-12 1978-01-03 Nalco Chemical Company Phospha-alumina gel and method of preparation
US4154812A (en) * 1977-03-25 1979-05-15 W. R. Grace & Co. Process for preparing alumina
US4560466A (en) * 1984-10-29 1985-12-24 Phillips Petroleum Company Hydrodemetallization of heavy oils in the presence of water
US4629716A (en) * 1985-04-15 1986-12-16 Shell Oil Company Process for producing narrow-pore catalyst supports
US4624938A (en) * 1985-04-26 1986-11-25 Shell Oil Company Process for producing wide-pore catalyst supports
US4629717A (en) * 1985-06-11 1986-12-16 Uop Inc. Phosphorus-modified alumina composite, method of manufacture and use thereof
US4588706A (en) * 1985-06-24 1986-05-13 Phillips Petroleum Company Phosphorus containing hydrofining catalysts

Also Published As

Publication number Publication date
CA1312594C (en) 1993-01-12
DE3762090D1 (de) 1990-05-10
JP2556340B2 (ja) 1996-11-20
EP0266008B1 (de) 1990-04-04
DK562187A (da) 1988-04-29
JPS63123444A (ja) 1988-05-27
EP0266008A1 (de) 1988-05-04
DK562187D0 (da) 1987-10-27
US4717707A (en) 1988-01-05

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