CA1029323A - Two stage metal-containing oil hydrodesulfurization process employing an activated alumina supported catalyst in each stage - Google Patents

Two stage metal-containing oil hydrodesulfurization process employing an activated alumina supported catalyst in each stage

Info

Publication number
CA1029323A
CA1029323A CA216,825A CA216825A CA1029323A CA 1029323 A CA1029323 A CA 1029323A CA 216825 A CA216825 A CA 216825A CA 1029323 A CA1029323 A CA 1029323A
Authority
CA
Canada
Prior art keywords
stage
supported catalyst
activated alumina
containing oil
process employing
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
CA216,825A
Other languages
English (en)
French (fr)
Other versions
CA216825S (en
Inventor
Harold Beuther
Angelo A. Montagna
Sun W. Chun
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.)
Gulf Research and Development Co
Original Assignee
Gulf Research and Development 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 Gulf Research and Development Co filed Critical Gulf Research and Development Co
Application granted granted Critical
Publication of CA1029323A publication Critical patent/CA1029323A/en
Expired 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
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
    • B01J21/04—Alumina
    • 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
    • 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
    • C10G45/10—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 platinum group metals or compounds thereof
    • 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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
CA216,825A 1974-04-24 1974-12-20 Two stage metal-containing oil hydrodesulfurization process employing an activated alumina supported catalyst in each stage Expired CA1029323A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US05/463,620 US3940330A (en) 1974-04-24 1974-04-24 Two stage metal-containing oil hydrodesulfurization process employing an activated alumina supported catalyst in each stage

Publications (1)

Publication Number Publication Date
CA1029323A true CA1029323A (en) 1978-04-11

Family

ID=23840740

Family Applications (1)

Application Number Title Priority Date Filing Date
CA216,825A Expired CA1029323A (en) 1974-04-24 1974-12-20 Two stage metal-containing oil hydrodesulfurization process employing an activated alumina supported catalyst in each stage

Country Status (3)

Country Link
US (1) US3940330A (cg-RX-API-DMAC7.html)
JP (1) JPS50148409A (cg-RX-API-DMAC7.html)
CA (1) CA1029323A (cg-RX-API-DMAC7.html)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4081353A (en) * 1976-10-15 1978-03-28 Gulf Research & Development Company Hydrodesulfurization with a specific alumina-supported catalyst
US4133777A (en) * 1977-06-28 1979-01-09 Gulf Research & Development Company Hydrodesulfurization catalyst
US4116818A (en) * 1977-06-28 1978-09-26 Gulf Research & Development Company Multi-reactor hydrodesulfurization process
AU3878395A (en) * 1994-11-25 1996-06-26 Kvaerner Process Technology Ltd. Multi-step hydrodesulfurization process
EP0944691A2 (en) * 1996-08-23 1999-09-29 Exxon Chemical Patents Inc. Heteroatom removal through countercurrent sorption
US5928497A (en) * 1997-08-22 1999-07-27 Exxon Chemical Pateuts Inc Heteroatom removal through countercurrent sorption
US6017443A (en) * 1998-02-05 2000-01-25 Mobil Oil Corporation Hydroprocessing process having staged reaction zones
US8894838B2 (en) 2011-04-29 2014-11-25 E I Du Pont De Nemours And Company Hydroprocessing process using uneven catalyst volume distribution among catalyst beds in liquid-full reactors
WO2014099242A1 (en) * 2012-12-21 2014-06-26 Exxonmobil Research And Engineering Company Hydroprocessing configuration for low sulfur diesel

Family Cites Families (4)

* 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
US3322666A (en) * 1964-08-25 1967-05-30 Gulf Research Development Co Chemical process for hydrocracking and hydrorefining of hydrocarbon oils
US3340180A (en) * 1964-08-25 1967-09-05 Gulf Research Development Co Hydrofining-hydrocracking process employing special alumina base catalysts
US3472759A (en) * 1967-04-25 1969-10-14 Atlantic Richfield Co Process for removal of sulfur and metals from petroleum materials

Also Published As

Publication number Publication date
US3940330A (en) 1976-02-24
JPS50148409A (cg-RX-API-DMAC7.html) 1975-11-28

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