GB1450700A - Process for the manufacture of technical and medicinal white oils - Google Patents

Process for the manufacture of technical and medicinal white oils

Info

Publication number
GB1450700A
GB1450700A GB5940573A GB5940573A GB1450700A GB 1450700 A GB1450700 A GB 1450700A GB 5940573 A GB5940573 A GB 5940573A GB 5940573 A GB5940573 A GB 5940573A GB 1450700 A GB1450700 A GB 1450700A
Authority
GB
United Kingdom
Prior art keywords
oils
oil
prepared
hydrogenation
technical
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
GB5940573A
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.)
BASF SE
Original Assignee
BASF SE
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 BASF SE filed Critical BASF SE
Publication of GB1450700A publication Critical patent/GB1450700A/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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/20—Sulfiding
    • 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
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14—Phosphorus; Compounds thereof
    • B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • B01J27/19—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
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/20—Carbon compounds
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/10—Lubricating oil

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)

Abstract

1450700 Hydrorefining oils BASF AG 21 Dec 1973 [2 Jan 1973] 59405/73 Heading C5E Technical white oil is made from a petroleum fraction which boils in the range 200‹ to 550‹ C. and contains aromatic compounds and nitrogencontaining, oxygen-containing, and sulphurcontaining compounds by catalytic hydrogenation using a catalyst which has been prepared by impregnating an alumina support, which can contain up to 5 wt. per cent silica, with a solution containing Ni<SP>2+</SP> cations, MoO 4 <SP>2-</SP> anions and PO 4 <SP>3-</SP> anions. This hydrogenation can be carried out at 250-370‹C and 30-200 atmospheres to prepare white oils, which can be used as printing ink oils or carrier oils for insecticides, from gas oil, spindle oil or lubricating oil. Medicinal white oil can be prepared from the technical white oils by hydrogenation in the presence of a base metal catalyst at 220- 330‹ C. and 50-250 atmospheres. The base metal catalyst can be one prepared by precipitating a material of the formula washing, compressing calcining and reduction with hydrogen to metallic nickel; it can be diluted with aluminium oxide of high surface area.
GB5940573A 1973-01-02 1973-12-21 Process for the manufacture of technical and medicinal white oils Expired GB1450700A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19732300038 DE2300038C2 (en) 1973-01-02 1973-01-02 Use of a sulfurized catalyst for the production of technical white oils

Publications (1)

Publication Number Publication Date
GB1450700A true GB1450700A (en) 1976-09-22

Family

ID=5868153

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5940573A Expired GB1450700A (en) 1973-01-02 1973-12-21 Process for the manufacture of technical and medicinal white oils

Country Status (6)

Country Link
BE (1) BE809334A (en)
DE (1) DE2300038C2 (en)
FR (1) FR2212417B1 (en)
GB (1) GB1450700A (en)
IT (1) IT1000171B (en)
NL (1) NL161496C (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2813571A1 (en) * 1977-03-30 1978-10-05 Exxon France WHITE OIL AND METHOD FOR PRODUCING IT
US5306847A (en) * 1991-11-26 1994-04-26 Basf Aktiengesellschaft Manufacture of 1,2-propylene glycol
US5561217A (en) * 1992-12-23 1996-10-01 Basf Aktiengesellschaft Preparation of polyether glycols
US5736484A (en) * 1994-03-15 1998-04-07 Basf Aktiengesellschaft Nickel-containing hydrogenation catalysts
US7321068B2 (en) 2003-12-09 2008-01-22 Basf Aktiengesellschaft Method for producing tricyclodecandialdehyde

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3143869A1 (en) * 1981-11-05 1983-05-11 Basf Ag, 6700 Ludwigshafen METHOD FOR PRODUCING TECHNICAL WHITE OILS BY HYDRATION
DE3570088D1 (en) * 1985-05-21 1989-06-15 Shell Int Research Single-stage hydrotreating process

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3287280A (en) * 1963-06-14 1966-11-22 American Cyanamid Co Hydrodesulfurization catalyst and process for preparing the same
FR1540296A (en) * 1967-01-31 1968-09-27 Exxon Standard Sa White oil manufacturing process
US3629146A (en) * 1969-03-24 1971-12-21 Shell Oil Co Catalyst impregnation method
GB1345972A (en) * 1971-06-23 1974-02-06 British Petroleum Co Production of white oils

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2813571A1 (en) * 1977-03-30 1978-10-05 Exxon France WHITE OIL AND METHOD FOR PRODUCING IT
US5306847A (en) * 1991-11-26 1994-04-26 Basf Aktiengesellschaft Manufacture of 1,2-propylene glycol
US5561217A (en) * 1992-12-23 1996-10-01 Basf Aktiengesellschaft Preparation of polyether glycols
US5736484A (en) * 1994-03-15 1998-04-07 Basf Aktiengesellschaft Nickel-containing hydrogenation catalysts
US7321068B2 (en) 2003-12-09 2008-01-22 Basf Aktiengesellschaft Method for producing tricyclodecandialdehyde

Also Published As

Publication number Publication date
DE2300038A1 (en) 1974-07-04
FR2212417A1 (en) 1974-07-26
NL7317792A (en) 1974-07-04
NL161496B (en) 1979-09-17
NL161496C (en) 1980-02-15
IT1000171B (en) 1976-03-30
DE2300038C2 (en) 1987-05-07
BE809334A (en) 1974-07-02
FR2212417B1 (en) 1980-03-14

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Legal Events

Date Code Title Description
PS Patent sealed
PE20 Patent expired after termination of 20 years

Effective date: 19931220