GB807581A - Production of alkynols and alkynediols - Google Patents

Production of alkynols and alkynediols

Info

Publication number
GB807581A
GB807581A GB33534/55A GB3353455A GB807581A GB 807581 A GB807581 A GB 807581A GB 33534/55 A GB33534/55 A GB 33534/55A GB 3353455 A GB3353455 A GB 3353455A GB 807581 A GB807581 A GB 807581A
Authority
GB
United Kingdom
Prior art keywords
carrier
heated
acetylene
per cent
kaolin
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
GB33534/55A
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.)
Fairweather Harold G C
Original Assignee
Fairweather Harold G C
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 Fairweather Harold G C filed Critical Fairweather Harold G C
Priority to GB33534/55A priority Critical patent/GB807581A/en
Publication of GB807581A publication Critical patent/GB807581A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/36Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring increasing the number of carbon atoms by reactions with formation of hydroxy groups, which may occur via intermediates being derivatives of hydroxy, e.g. O-metal
    • C07C29/38Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring increasing the number of carbon atoms by reactions with formation of hydroxy groups, which may occur via intermediates being derivatives of hydroxy, e.g. O-metal by reaction with aldehydes or ketones
    • C07C29/42Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring increasing the number of carbon atoms by reactions with formation of hydroxy groups, which may occur via intermediates being derivatives of hydroxy, e.g. O-metal by reaction with aldehydes or ketones with compounds containing triple carbon-to-carbon bonds, e.g. with metal-alkynes
    • 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
    • B01J23/72Copper
    • 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
    • B01J23/843Arsenic, antimony or bismuth
    • B01J23/8437Bismuth

Landscapes

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

Abstract

Alkynols (including alkyndiols) are made by reacting aldehydes or ketones with acetylene (see Group IV (b)) in the presence of a catalyst made by depositing copper oxide on a siliceous carrier which is then heated to a temperature of 400 DEG to 800 DEG C., by which a surface layer of copper silicate is formed. Preferably a little bismuth oxide is present with the copper oxide. The metal silicate prevents the formation of cuprene. Kaolin, silica gel, or fuller's earth may be used as the carrier, but preferably kaolin is mixed with an organic binder, formed into shapes and roasted at 800 DEG to 850 DEG C. to burn out the binder, and finally heated at 1000 DEG to 1200 DEG C. to impart a mullite-like structure. Binders specified are, polyacrylic acid, alginic or pectic acid, polyvinyl methyl ether or methyl cellulose. In examples, the calcined carrier is impregnated with a solution containing copper nitrate or nitrite, bismuth nitrate and dilute nitric acid. The pulp is extruded, and the shaped pieces dried and finally heated at 400 DEG to 800 DEG C. for 5 to 34 hours. The bismuth compound may be replaced by compounds of Au, Hg, Pb, Se, Ce, or of halogens. U.S.A. Specifications 2,232,867 and 2,300,969 are referred to.ALSO:Alkynols (including alkyndiols) are made by reacting aldehydes or ketones with acetylene in the presence of a catalyst made by depositing copper oxide on a siliceous carrier which is then heated to a temperature of 400 DEG to 800 DEG C., by which a surface coating of copper silicate is formed, thus preventing the formation of cuprene. Preferably, there is also present a small amount of an oxide of Bi, Au, Hg, Pb, Se or Ce. Kaolin, silica gel, or fuller's earth are used as carrier, but preferably kaolin is mixed with a polymeric organic binder, the mixture formed into shapes, dried, calcined and then impregnated with solutions of the metal salts and re-ignited (see Group III). In examples, a long tubular reactor column packed with the catalyst is first flushed with nitrogen, and then heated to 90 DEG C., while a 6 per cent formaldehyde solution trickles downwards through the column. Acetylene is bled into the nitrogen feed increasing to a concentration of 70 per cent acetylene, and also the temperature is raised to 120 DEG C. The concentration of formaldehyde is also raised to 18.5 per cent. The gases produced are condensed, surplus gases recycled, and water removed from the condensate, which is then submitted to azeotropic distillation. In a 600 hour operation, 80 per cent of the formaldehyde is converted to alkyne diol. U.S.A. Specifications 2,232,867, 2,300,969 and 2,527,358 are referred to.
GB33534/55A 1955-11-23 1955-11-23 Production of alkynols and alkynediols Expired GB807581A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB33534/55A GB807581A (en) 1955-11-23 1955-11-23 Production of alkynols and alkynediols

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB33534/55A GB807581A (en) 1955-11-23 1955-11-23 Production of alkynols and alkynediols

Publications (1)

Publication Number Publication Date
GB807581A true GB807581A (en) 1959-01-21

Family

ID=10354201

Family Applications (1)

Application Number Title Priority Date Filing Date
GB33534/55A Expired GB807581A (en) 1955-11-23 1955-11-23 Production of alkynols and alkynediols

Country Status (1)

Country Link
GB (1) GB807581A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4085151A (en) * 1977-06-29 1978-04-18 E. I. Du Pont De Nemours And Company Butynediol production
CN113751039A (en) * 2021-09-17 2021-12-07 山西大学 Alkynylation catalyst for synthesizing propiolic alcohol, preparation method and application
CN113813973A (en) * 2021-09-17 2021-12-21 山西大学 Nano gold confinement copper-based core-shell structure catalyst and preparation method and application thereof
CN117205934A (en) * 2023-11-09 2023-12-12 山东嘉虹化工有限公司 Copper bismuth catalyst and preparation method thereof

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4085151A (en) * 1977-06-29 1978-04-18 E. I. Du Pont De Nemours And Company Butynediol production
CN113751039A (en) * 2021-09-17 2021-12-07 山西大学 Alkynylation catalyst for synthesizing propiolic alcohol, preparation method and application
CN113813973A (en) * 2021-09-17 2021-12-21 山西大学 Nano gold confinement copper-based core-shell structure catalyst and preparation method and application thereof
CN113751039B (en) * 2021-09-17 2022-07-19 山西大学 Alkynylation catalyst for synthesizing propiolic alcohol, preparation method and application
CN113813973B (en) * 2021-09-17 2023-03-10 山西大学 Nano gold confinement copper-based core-shell structure catalyst and preparation method and application thereof
CN117205934A (en) * 2023-11-09 2023-12-12 山东嘉虹化工有限公司 Copper bismuth catalyst and preparation method thereof
CN117205934B (en) * 2023-11-09 2024-01-02 山东嘉虹化工有限公司 Copper bismuth catalyst and preparation method thereof

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