GB1415417A - Hydrotreating of petroleum distillates using shaped catalyst prtticles - Google Patents

Hydrotreating of petroleum distillates using shaped catalyst prtticles

Info

Publication number
GB1415417A
GB1415417A GB4789973A GB4789973A GB1415417A GB 1415417 A GB1415417 A GB 1415417A GB 4789973 A GB4789973 A GB 4789973A GB 4789973 A GB4789973 A GB 4789973A GB 1415417 A GB1415417 A GB 1415417A
Authority
GB
United Kingdom
Prior art keywords
particles
catalyst
hydrotreating
inch
petroleum distillates
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
Application number
GB4789973A
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.)
Wyeth Holdings LLC
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
Application filed by American Cyanamid Co filed Critical American Cyanamid Co
Priority to GB4789973A priority Critical patent/GB1415417A/en
Priority to DE19732354330 priority patent/DE2354330A1/en
Priority to FR7338687A priority patent/FR2249160B1/fr
Priority to NL7315061A priority patent/NL7315061A/en
Publication of GB1415417A publication Critical patent/GB1415417A/en
Priority to MY1978192A priority patent/MY7800192A/en
Expired legal-status Critical Current

Links

Classifications

    • B01J35/50—
    • 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
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/076—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J35/60—
    • 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
    • B01J37/20—Sulfiding
    • 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
    • B01J35/615—
    • B01J35/633—
    • B01J35/635—
    • B01J35/647—

Abstract

1415417 Shaped hydrotreating catalyst AMERICAN CYANAMID CO 12 Oct 1973 47899/73 Heading B1E [Also in Divisions C4 and C5] A catalyst for use in hydrotreating petroleum distillates comprises porous, but non-hollow; particles having a polylobal cross-sectional shape characterised by a concavity index greater than 1.0, a void fraction of 0.25 to 0.60, a ratio of geometric volume to geometric surface in the range 0.001 to 0.042 inch, a catalytic surface area greater than 100 m<SP>2</SP>/g, a catalytic pore volume of 0.35 to 0.65 cc/g which results from a major portion of pores of diameter 40 to 90Š when measured with mercury up to 50000 psi abs. and a contact angle of 140‹, and when containing more than two lobes at least 15% of the points within the particles are greater than 0.015 inch from the particle surface and a composition cmprising a major portion by weight of alumina, 5 to 25% molybdenum oxide and 1-8% of cobalt and/or nickel oxides. In examples catalyst particles are formed by extruding alumina powder which has been moistened with aqueous ammonium molybdate and cobalt nitrate in "dumbell" or "3 leaf clover" cross sections and presulphiding. The catalyst particles can also have cross sections corresponding to a Figure of eight and tetralobal rods.
GB4789973A 1973-10-12 1973-10-12 Hydrotreating of petroleum distillates using shaped catalyst prtticles Expired GB1415417A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
GB4789973A GB1415417A (en) 1973-10-12 1973-10-12 Hydrotreating of petroleum distillates using shaped catalyst prtticles
DE19732354330 DE2354330A1 (en) 1973-10-12 1973-10-30 METHOD FOR TREATMENT OF PETROLEUM DISTILLATES WITH HYDROGEN IN THE PRESENCE OF SHAPED CATALYST PARTICLES
FR7338687A FR2249160B1 (en) 1973-10-12 1973-10-30
NL7315061A NL7315061A (en) 1973-10-12 1973-11-02 PROCEDURE FOR PREPARING CATALYSTS.
MY1978192A MY7800192A (en) 1973-10-12 1978-12-31 Hydrotreating of petroleum distillates using shaped catalyst particles

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
GB4789973A GB1415417A (en) 1973-10-12 1973-10-12 Hydrotreating of petroleum distillates using shaped catalyst prtticles
DE19732354330 DE2354330A1 (en) 1973-10-12 1973-10-30 METHOD FOR TREATMENT OF PETROLEUM DISTILLATES WITH HYDROGEN IN THE PRESENCE OF SHAPED CATALYST PARTICLES
FR7338687A FR2249160B1 (en) 1973-10-12 1973-10-30
NL7315061A NL7315061A (en) 1973-10-12 1973-11-02 PROCEDURE FOR PREPARING CATALYSTS.

Publications (1)

Publication Number Publication Date
GB1415417A true GB1415417A (en) 1975-11-26

Family

ID=27431761

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4789973A Expired GB1415417A (en) 1973-10-12 1973-10-12 Hydrotreating of petroleum distillates using shaped catalyst prtticles

Country Status (5)

Country Link
DE (1) DE2354330A1 (en)
FR (1) FR2249160B1 (en)
GB (1) GB1415417A (en)
MY (1) MY7800192A (en)
NL (1) NL7315061A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0013980A1 (en) * 1979-01-27 1980-08-06 BASF Aktiengesellschaft Use of cobalt-molybdene and/or nickel-molybdeneoxide catalysts for the hydrorefining of petroleum hydrocarbons
US6863436B2 (en) 2001-12-19 2005-03-08 Eta Sa Fabriques D'ebauches Watch including a casing ring for a movement mounted in a case assembled via the bezel or via the back cover
EP1800750A2 (en) * 2005-12-22 2007-06-27 Institut Français du Pétrole Method of selective hydrogenation using a catalyst with controlled porosity
EP1800748A2 (en) * 2005-12-22 2007-06-27 Institut Français du Pétrole Method of selective hydrogenation using a sulphided catalyst
EP1800749A2 (en) * 2005-12-22 2007-06-27 Institut Francais Du Petrole Method of selective hydrogenation using a catalyst with a specific support

Family Cites Families (5)

* 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
US3509044A (en) * 1967-06-26 1970-04-28 Exxon Research Engineering Co Hydrodesulfurization of petroleum residuum
US3630888A (en) * 1970-03-02 1971-12-28 Hydrocarbon Research Inc Hydrocracking and desulfurization with a catalyst having
US3674680A (en) * 1970-03-09 1972-07-04 Standard Oil Co Process and catalyst for hydroprocessing a resid hydrocarbon
US3732155A (en) * 1971-03-31 1973-05-08 Exxon Research Engineering Co Two-stage hydrodesulfurization process with hydrogen addition in the first stage

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0013980A1 (en) * 1979-01-27 1980-08-06 BASF Aktiengesellschaft Use of cobalt-molybdene and/or nickel-molybdeneoxide catalysts for the hydrorefining of petroleum hydrocarbons
US6863436B2 (en) 2001-12-19 2005-03-08 Eta Sa Fabriques D'ebauches Watch including a casing ring for a movement mounted in a case assembled via the bezel or via the back cover
EP1800750A2 (en) * 2005-12-22 2007-06-27 Institut Français du Pétrole Method of selective hydrogenation using a catalyst with controlled porosity
EP1800748A2 (en) * 2005-12-22 2007-06-27 Institut Français du Pétrole Method of selective hydrogenation using a sulphided catalyst
EP1800749A2 (en) * 2005-12-22 2007-06-27 Institut Francais Du Petrole Method of selective hydrogenation using a catalyst with a specific support
FR2895414A1 (en) * 2005-12-22 2007-06-29 Inst Francais Du Petrole SELECTIVE HYDROGENATION PROCESS IMPLEMENTING A CATALYST WITH CONTROLLED POROSITY
FR2895416A1 (en) * 2005-12-22 2007-06-29 Inst Francais Du Petrole SELECTIVE HYDROGENATION PROCESS USING A SULPHIDE CATALYST
FR2895415A1 (en) * 2005-12-22 2007-06-29 Inst Francais Du Petrole SELECTIVE HYDROGENATION PROCESS IMPLEMENTING A CATALYST WITH A SPECIFIC SUPPORT
US7645376B2 (en) 2005-12-22 2010-01-12 Institute Francais Du Petrole Selective hydrogenation process employing a sulphurized catalyst
US7718053B2 (en) 2005-12-22 2010-05-18 Institut Francais Du Petrole Selective hydrogenation process employing a catalyst having a controlled porosity
US7736492B2 (en) 2005-12-22 2010-06-15 Institut Francais Du Petrole Selective hydrogenation process employing a catalyst with a specific support
EP1800750A3 (en) * 2005-12-22 2011-04-20 Institut Français du Pétrole Method of selective hydrogenation using a catalyst with controlled porosity
EP1800748A3 (en) * 2005-12-22 2011-04-20 Institut Français du Pétrole Method of selective hydrogenation using a sulphided catalyst
EP1800749A3 (en) * 2005-12-22 2011-04-20 Institut Français du Pétrole Method of selective hydrogenation using a catalyst with a specific support

Also Published As

Publication number Publication date
NL7315061A (en) 1975-05-07
DE2354330C2 (en) 1987-11-19
MY7800192A (en) 1978-12-31
FR2249160A1 (en) 1975-05-23
FR2249160B1 (en) 1979-07-20
DE2354330A1 (en) 1975-05-07

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PE20 Patent expired after termination of 20 years

Effective date: 19931011