GB625909A - Manufacture of polyhydroxy compounds - Google Patents

Manufacture of polyhydroxy compounds

Info

Publication number
GB625909A
GB625909A GB24122/46A GB2412246A GB625909A GB 625909 A GB625909 A GB 625909A GB 24122/46 A GB24122/46 A GB 24122/46A GB 2412246 A GB2412246 A GB 2412246A GB 625909 A GB625909 A GB 625909A
Authority
GB
United Kingdom
Prior art keywords
mixture
pressure
atmospheres
hydrogen
carbon monoxide
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
GB24122/46A
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.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and 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 EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Priority to GB24122/46A priority Critical patent/GB625909A/en
Publication of GB625909A publication Critical patent/GB625909A/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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

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

Abstract

Polyhydroxy compounds are produced by reacting a mixture of formaldehyde, carbon monoxide and hydrogen, the formaldehyde being initially present, at a pressure of not less than 200 atmospheres and at a temperature of from 80 to 300 DEG C. in the presence of a hydrogenating catalyst. Instead of formaldehyde compounds yielding it under the reaction conditions may be used, e.g. paraformaldehyde, reactive formals, trioxane, and N-methylol derivatives. The reaction products may be further treated with hydrogen to obtain increased yields of hydroxy compounds boiling in the range of the lower glycols, and glycerine. This subsequent hydrogenation may be conducted in the presence of a hydrogenation catalyst, e.g. copper chromite at superatmospheric pressure at a temperature of about 100 DEG to 300 DEG C. Specified hydrogenating catalysts for the main reaction are nickel, cobalt, manganese, iron, chromium, copper, platinum, molybdenum, palladium, zinc, cadmium, ruthenium and compounds thereof or combinations of these materials with each other or with inert supports, e.g. kieselguhr, pumice, or with promoters such as thoria and manganese. Preferred catalysts are cobalt-containing catalysts such as metallic cobalt, reduced sintered cobalt oxide, cobalt carbonyl and salts of cobalt. Preferred temperatures are 100 DEG to 200 DEG C. and pressures of 200 to 1500 atmospheres are preferred. The reaction may be effected in an inert reaction medium, e.g. an aliphatic ether or ester. In examples: (1) a mixture of paraformaldehyde, methyl formate and reduced sintered cobalt oxide is heated in a silver-lined shaker tube under a pressure of 500 to 700 atmospheres of a mixture of carbon monoxide and hydrogen, distillation of the resulting mixture yields a mixture of polyhydroxy compounds; (2) reaction is effected as in (1) but a pressure of 460 to 750 atmospheres is employed, the resulting product is freed from methyl formate and then hydrogenated in methanol solution in the presence of copper chromite at a temperature of 230 DEG C. under a pressure of 745 to 750 atmospheres. Distillation of the product yields fractions containing ethylene glycol and glycerol respectively; (3) a mixture of trioxane, distilled water and reduced sintered cobalt oxide are heated under a pressure of 550 to 640 atmospheres of a gas containing carbon monoxide and hydrogen and the resulting product distilled yielding polyhydroxy compounds; (4) a mixture of paraformaldehyde, methyl formate, and reduced sintered cobalt oxide is heated under pressure and a mixture of carbon monoxide and hydrogen is then injected and the heating continued under a pressure of 445 to 735 atmospheres. Distillation of the product gives a syrupy residue containing polyhydroxy compounds and unspecified oxygenated compounds. The molecular ratio of carbon monoxide to hydrogen used is preferably from 4 : 1 to 1 : 10 and in the examples about 1.5 to 2 moles of carbon monoxide is initially present per mole of formaldehyde.
GB24122/46A 1946-08-14 1946-08-14 Manufacture of polyhydroxy compounds Expired GB625909A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB24122/46A GB625909A (en) 1946-08-14 1946-08-14 Manufacture of polyhydroxy compounds

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB24122/46A GB625909A (en) 1946-08-14 1946-08-14 Manufacture of polyhydroxy compounds

Publications (1)

Publication Number Publication Date
GB625909A true GB625909A (en) 1949-07-06

Family

ID=10206739

Family Applications (1)

Application Number Title Priority Date Filing Date
GB24122/46A Expired GB625909A (en) 1946-08-14 1946-08-14 Manufacture of polyhydroxy compounds

Country Status (1)

Country Link
GB (1) GB625909A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2757202A (en) * 1952-03-22 1956-07-31 Exxon Research Engineering Co Aldehyde synthesis process
FR2375172A1 (en) * 1976-10-21 1978-07-21 Chevron Res Catalytic prepn. of ethylene glycol from formaldehyde - with carbon monoxide and hydrogen using a rhodium cpd. catalyst
US4533774A (en) * 1982-11-27 1985-08-06 The British Petroleum Company P.L.C. Process for the production of ethylene glycol

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2757202A (en) * 1952-03-22 1956-07-31 Exxon Research Engineering Co Aldehyde synthesis process
FR2375172A1 (en) * 1976-10-21 1978-07-21 Chevron Res Catalytic prepn. of ethylene glycol from formaldehyde - with carbon monoxide and hydrogen using a rhodium cpd. catalyst
US4533774A (en) * 1982-11-27 1985-08-06 The British Petroleum Company P.L.C. Process for the production of ethylene glycol

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