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GB396681A - An improved method of preparing catalytic materials - Google Patents

An improved method of preparing catalytic materials

Info

Publication number
GB396681A
GB396681A GB30769/31A GB3076931A GB396681A GB 396681 A GB396681 A GB 396681A GB 30769/31 A GB30769/31 A GB 30769/31A GB 3076931 A GB3076931 A GB 3076931A GB 396681 A GB396681 A GB 396681A
Authority
GB
United Kingdom
Prior art keywords
acid
per cent
lumps
precipitated
mixed
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
GB30769/31A
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.)
Standard Oil Development Co
Original Assignee
Standard Oil 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 Standard Oil Development Co filed Critical Standard Oil Development Co
Publication of GB396681A publication Critical patent/GB396681A/en
Expired 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
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/24Chromium, molybdenum or tungsten
    • B01J23/28Molybdenum
    • 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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/08Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal with moving catalysts
    • C10G1/086Characterised by the catalyst used

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)

Abstract

A catalyst for the hydrogenation of carbonaceous materials, especially under high pressure, is obtained by dissolving molybdic acid in an alkali, preferably a 6-7 per cent solution of ammonia, and concentrating the resulting solution to a specific gravity greater than 1,0, and preferably between about 1,2 and 1,4. The molybdic acid is then precipitated by means of an acid such as hydrochloric acid which is added until the mixture contains an excess of 1-4 per cent, preferably about 3 per cent. If other acids are used, the hydrogen ion concentration of the resulting mixture should be substantially equivalent to that of mixtures containing the above excess of hydrochloric acid. The precipitated acid is then separated, washed with water or ammonium chloride solution, and dried at 200-212 DEG F. The acid is then heated at an elevated temperature until rodshaped crystals of the desired size are formed. Temperatures between 750-1500 DEG F. may be used, but between 780-840 DEG F. are preferred. The molybdic acid thus prepared may be moulded into shapes, or mixed with a bonding agent such as magnesium or zinc oxides and pressed into lumps. It may also be mixed with other catalytic materials such as tungsten or chromium oxides or sulphides, or may be deposited on inert materials having a large surface, such as alumina, silica, pumice or active charcoal. The catalyst mixtures may be used in the form of lumps or be finely ground and suspended in the material to be treated.
GB30769/31A 1930-11-29 1931-11-06 An improved method of preparing catalytic materials Expired GB396681A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US396681XA 1930-11-29 1930-11-29

Publications (1)

Publication Number Publication Date
GB396681A true GB396681A (en) 1933-08-10

Family

ID=21906721

Family Applications (1)

Application Number Title Priority Date Filing Date
GB30769/31A Expired GB396681A (en) 1930-11-29 1931-11-06 An improved method of preparing catalytic materials

Country Status (1)

Country Link
GB (1) GB396681A (en)

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