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GB814073A - Catalytic oxidation of methanol and catalyst and catalyst precursor therefor - Google Patents

Catalytic oxidation of methanol and catalyst and catalyst precursor therefor

Info

Publication number
GB814073A
GB814073A GB24129/55A GB2412955A GB814073A GB 814073 A GB814073 A GB 814073A GB 24129/55 A GB24129/55 A GB 24129/55A GB 2412955 A GB2412955 A GB 2412955A GB 814073 A GB814073 A GB 814073A
Authority
GB
United Kingdom
Prior art keywords
precipitate
catalyst
solution
molybdate
methanol
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
GB24129/55A
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.)
Reichhold Chemicals Inc
Original Assignee
Reichhold Chemicals Inc
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 Reichhold Chemicals Inc filed Critical Reichhold Chemicals Inc
Publication of GB814073A publication Critical patent/GB814073A/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
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C47/00Compounds having —CHO groups
    • C07C47/02Saturated compounds having —CHO groups bound to acyclic carbon atoms or to hydrogen
    • C07C47/04Formaldehyde

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

An inactive catalyst precursor suitable for conversion to an active catalyst for the oxidation of methanol to formaldehyde (see Group IV (b)) is prepared by mixing an aqueous solution of an iron salt with an aqueous solution of a molybdate and partially drying the precipitate; the mixture of solutions should have a pH of 0.5-3.5 and the precipitate a molar ratio of MoO3 to Fe2O3 of 3.3:1 to 11.2:1. The catalyst precursor has good mechanical strength and is stable during storage and transport. Suitable iron salts are ferric chloride, bromide, acetate, and sulphate and ferrous chloride and acetate; suitable molybdates are ammonium, potassium, and sodium molybdates, and molybdates of organic amines. Trace amounts of Al, Ca, Cr, Co, Mg, Ni and Si in the catalyst precursor are not harmful. The molybdate solution should preferably be adjusted to a pH of 2.25 to 5.0 by addition of hydrochloric or hydrobromic acid. After washing and filtering the precipitate is dried, preferably in stages at increasing temperatures up to 300 DEG F. to a water content of 2-30 per cent. In examples: (1) a solution of sodium molybdate, made by dissolving molybdenum trioxide in sodium hydroxide solution, is treated with concentrated hydrochloric acid to a pH of 5 and then added to ferric chloride solution of pH 1.7; the precipitate is washed, filtered and dried; (2) a solution of ammonium molybdate is adjusted to pH 2.25 with hydrochloric acid and is added to ferric chloride solution, the precipitate being treated as in (1). In each example the product is loaded into the tubes of a converter and an active catalyst formed by heating to a temperature of 500 DEG F. in a stream of air, which may be dehydrated, until all water and volatile substances are removed. U.S.A. Specification 1,913,405 is referred to.ALSO:Formaldehyde is prepared by passing methanol and an oxidizing gas through a catalyst formed by heating at 300-495 DEG F. in the presence of air a catalyst precursor which has been produced by mixing an aqueous solution of an iron salt with an aqueous solution of a molybdate and partially drying the precipitate; the mixture of solutions should have a pH of 0.5-3.5 and the precipitate a molar ratio of MoO3 to Fe2O3 of 3.3 : 1 to 11.2 : 1 (see Group III). A mixture of 9 per cent methanol and 91 per cent air may be passed at 480 DEG F. through parallel tubes containing the catalyst. A suitable arrangement of apparatus is shown diagrammatically. U.S.A. Specification 1,913,405 is referred to.
GB24129/55A 1954-08-27 1955-08-22 Catalytic oxidation of methanol and catalyst and catalyst precursor therefor Expired GB814073A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US814073XA 1954-08-27 1954-08-27

Publications (1)

Publication Number Publication Date
GB814073A true GB814073A (en) 1959-05-27

Family

ID=22163956

Family Applications (1)

Application Number Title Priority Date Filing Date
GB24129/55A Expired GB814073A (en) 1954-08-27 1955-08-22 Catalytic oxidation of methanol and catalyst and catalyst precursor therefor

Country Status (1)

Country Link
GB (1) GB814073A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0109775A1 (en) * 1982-10-26 1984-05-30 Nitto Chemical Industry Co., Ltd. Process for regeneration of iron-antimony metallic oxide catalysts

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0109775A1 (en) * 1982-10-26 1984-05-30 Nitto Chemical Industry Co., Ltd. Process for regeneration of iron-antimony metallic oxide catalysts

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