GB698019A - Di-hydric alcohols - Google Patents

Di-hydric alcohols

Info

Publication number
GB698019A
GB698019A GB25108/51A GB2510851A GB698019A GB 698019 A GB698019 A GB 698019A GB 25108/51 A GB25108/51 A GB 25108/51A GB 2510851 A GB2510851 A GB 2510851A GB 698019 A GB698019 A GB 698019A
Authority
GB
United Kingdom
Prior art keywords
catalyst
reaction
acetylene
diol
solution
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
GB25108/51A
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.)
Celanese Corp
Original Assignee
Celanese Corp
Celanese Corp of America
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 Celanese Corp, Celanese Corp of America filed Critical Celanese Corp
Publication of GB698019A publication Critical patent/GB698019A/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

Landscapes

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

Abstract

Alkine diols are continuously produced by a liquid phase reaction between acetylene and an aldehyde or ketone, in which a copper acetylide catalyst is maintained in suspension in the liquid reaction medium in the form of a slurry by the continuous passage of acetylene upwards through the medium, a quiescent zone is maintained in the reaction mixture from which zone liquid is continuously withdrawn, and fresh aldehyde or ketone is supplied to maintain the volume of reaction liquid constant. The quiescent zone in the reaction medium can be effected by providing a baffled zone near the top of the reactor and this ensures that substantially no catalyst is withdrawn in the crude product being removed. The catalyst preferably comprises copper acetylide supported on silica gel. Preferably a catalyst of a particle size between 50 and 100 mesh is used. The reaction is preferably carried out at a temperature between 180 DEG and 220 DEG F. The alkine diol produced may be hydrogenated to give the alkane diol at temperatures of 210-300 DEG F. and a pressure of 800 to 1800 lb. per square inch in the presence of Raney nickel at a pH value between 7 and 8. In the example, a copper acetylide catalyst deposited on silica gel is suspended in an aqueous formaldehyde solution; acetylene and aqueous formaldehyde solution are continuously introduced into the reaction, the acetylene being introduced at such a rate as to keep the catalyst in suspension; the overflow of aqueous formaldehyde solution containing 1.4-butine diol is continuously removed from the zone at the top of the reactor where baffles are provided to maintain the reaction liquid in a quiescent state. The crude aqueous solution of 1.4-butine diol is steam stripped and distilled to give a solution of 1.4-butine diol which is subsequently hydrogenated to give a solution of 1.4-butane diol, which is purified by distilling and extracting with 2 ethyl hexanol.ALSO:A catalyst for the reaction between acetylene and an aldehyde p or ketone to produce alkine diols consists of a copper acetylide, preferably supported on silica gel. In an example silica gel is mixed with a solution of copper nitrate and bismuth nitrate in dilute nitric acid; the mixture is dried, calcined, reduced with formaldehyde and then treated with acetylene to give a an acetylide-acetylene complex which is the active catalyst.
GB25108/51A 1950-10-28 1951-10-26 Di-hydric alcohols Expired GB698019A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US698019XA 1950-10-28 1950-10-28

Publications (1)

Publication Number Publication Date
GB698019A true GB698019A (en) 1953-10-07

Family

ID=22091296

Family Applications (1)

Application Number Title Priority Date Filing Date
GB25108/51A Expired GB698019A (en) 1950-10-28 1951-10-26 Di-hydric alcohols

Country Status (1)

Country Link
GB (1) GB698019A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2908722A (en) * 1956-09-07 1959-10-13 Air Reduction Process for preparing saturated monohydric alcohols
US2967893A (en) * 1958-12-30 1961-01-10 Gen Aniline & Film Corp Hydrogenation of 2-butyne-1, 4-diol to 1, 4-butanediol
US2993078A (en) * 1958-12-22 1961-07-18 Gen Aniline & Film Corp Purification of butynediol
US3154589A (en) * 1960-06-27 1964-10-27 Allied Chem Process for butynediol
US3691093A (en) * 1969-02-12 1972-09-12 Du Pont Efficiency of nickel-aluminum catalysts by water washing
US3957888A (en) * 1974-05-03 1976-05-18 Basf Aktiengesellschaft Process for the manufacture of butynediol
US4085151A (en) * 1977-06-29 1978-04-18 E. I. Du Pont De Nemours And Company Butynediol production
US4093668A (en) * 1973-03-24 1978-06-06 Basf Aktiengesellschaft Manufacture of butynediol
US4373999A (en) * 1981-04-08 1983-02-15 Gaf-Huls Chemie Gmbh Distillation of butinediol-1,4
US4584418A (en) * 1985-03-15 1986-04-22 E. I. Du Pont De Nemours And Company Preparation of butynediol

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2908722A (en) * 1956-09-07 1959-10-13 Air Reduction Process for preparing saturated monohydric alcohols
US2993078A (en) * 1958-12-22 1961-07-18 Gen Aniline & Film Corp Purification of butynediol
US2967893A (en) * 1958-12-30 1961-01-10 Gen Aniline & Film Corp Hydrogenation of 2-butyne-1, 4-diol to 1, 4-butanediol
US3154589A (en) * 1960-06-27 1964-10-27 Allied Chem Process for butynediol
US3691093A (en) * 1969-02-12 1972-09-12 Du Pont Efficiency of nickel-aluminum catalysts by water washing
US4093668A (en) * 1973-03-24 1978-06-06 Basf Aktiengesellschaft Manufacture of butynediol
US3957888A (en) * 1974-05-03 1976-05-18 Basf Aktiengesellschaft Process for the manufacture of butynediol
US4085151A (en) * 1977-06-29 1978-04-18 E. I. Du Pont De Nemours And Company Butynediol production
US4373999A (en) * 1981-04-08 1983-02-15 Gaf-Huls Chemie Gmbh Distillation of butinediol-1,4
US4584418A (en) * 1985-03-15 1986-04-22 E. I. Du Pont De Nemours And Company Preparation of butynediol

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