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GB833577A - Process for the manufacture of catalysts - Google Patents

Process for the manufacture of catalysts

Info

Publication number
GB833577A
GB833577A GB1184757A GB1184757A GB833577A GB 833577 A GB833577 A GB 833577A GB 1184757 A GB1184757 A GB 1184757A GB 1184757 A GB1184757 A GB 1184757A GB 833577 A GB833577 A GB 833577A
Authority
GB
United Kingdom
Prior art keywords
product
compound
stage
aqueous solution
impregnating
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
GB1184757A
Inventor
Douglas August Charles D Rycke
Edwin Bolwell Andrews
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.)
Peter Spence and Sons Ltd
Original Assignee
Peter Spence and Sons Ltd
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 Peter Spence and Sons Ltd filed Critical Peter Spence and Sons Ltd
Priority to GB1184757A priority Critical patent/GB833577A/en
Publication of GB833577A publication Critical patent/GB833577A/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
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts 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
    • B01J23/84Catalysts 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
    • B01J23/85Chromium, molybdenum or tungsten
    • B01J23/86Chromium
    • B01J23/862Iron and chromium
    • 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
    • B01J23/26Chromium

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Catalysts (AREA)

Abstract

A promoted chromia-alumina catalyst is prepared by (1) reacting aluminium sulphate or aluminium ammonium sulphate with an alkaline precipitant (preferably an aqueous solution of (a) ammonia or (b) sodium aluminate) under conditions effective to form a substantially granular hydrogel precipitate; (2) optionally washing the precipitate; (3) transforming it into a gel, preferably by passing through a colloid mill, particularly wherein the apertures are between 0.001 and 0.005 inch; (4) spray drying the gel under conditions effective to produce microspheroids of relatively uniform size distribution (preferably a chamber spray drier of the rotating disc type is used); (5) washing the product if stage (2) was omitted, preferably with dilute aqueous ammonia and particularly subsequently with water; (6) roasting the dried product at 500-700 DEG C., preferably 600 DEG C.; (7) impregnating with an aqueous solution comprising a compound of chromium and either a compound each of cerium (the technical material containing other lanthanons may be used) and potassium or a compound of iron, nickel or cobalt; (8) separating the impregnated product from any superfluous impregnating solution; and (9) calcinating the impregnated product to decompose the compounds of the active elements into their oxides, preferably at approximately 550 DEG C. For stage (7), one of the following alternatives is preferred:-either the impregnating solution comprises chromic acid and copperas, or the product of the roasting stage is introduced into an aqueous solution containing chromic acid, cerous nitrate and potassium nitrate.
GB1184757A 1957-04-11 1957-04-11 Process for the manufacture of catalysts Expired GB833577A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1184757A GB833577A (en) 1957-04-11 1957-04-11 Process for the manufacture of catalysts

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1184757A GB833577A (en) 1957-04-11 1957-04-11 Process for the manufacture of catalysts

Publications (1)

Publication Number Publication Date
GB833577A true GB833577A (en) 1960-04-27

Family

ID=9993777

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1184757A Expired GB833577A (en) 1957-04-11 1957-04-11 Process for the manufacture of catalysts

Country Status (1)

Country Link
GB (1) GB833577A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112547061A (en) * 2019-09-25 2021-03-26 中国石油化工股份有限公司 Catalyst for preparing propylene by propane dehydrogenation and preparation method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112547061A (en) * 2019-09-25 2021-03-26 中国石油化工股份有限公司 Catalyst for preparing propylene by propane dehydrogenation and preparation method thereof

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