GB600454A - Improvements in or relating to the production of acrolein - Google Patents

Improvements in or relating to the production of acrolein

Info

Publication number
GB600454A
GB600454A GB1852643A GB1852643A GB600454A GB 600454 A GB600454 A GB 600454A GB 1852643 A GB1852643 A GB 1852643A GB 1852643 A GB1852643 A GB 1852643A GB 600454 A GB600454 A GB 600454A
Authority
GB
United Kingdom
Prior art keywords
paraldehyde
acetaldehyde
acrolein
reaction
crotonaldehyde
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
GB1852643A
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.)
Distillers Co Yeast Ltd
Distillers Co Ltd
Original Assignee
Distillers Co Yeast Ltd
Distillers Co Ltd
Filing date
Publication date
Application filed by Distillers Co Yeast Ltd, Distillers Co Ltd filed Critical Distillers Co Yeast Ltd
Publication of GB600454A publication Critical patent/GB600454A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/61Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
    • C07C45/67Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton
    • C07C45/68Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms
    • C07C45/72Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms by reaction of compounds containing >C = O groups with the same or other compounds containing >C = O groups
    • C07C45/75Reactions with formaldehyde

Landscapes

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

Abstract

A process for the production of acrolein by the vapour phase reaction at 280-300 DEG C. of formaldehyde and acetaldehyde in the presence of a dehydrating catalyst comprises replacing from 25 to 80 per cent by weight of the acetaldehyde admitted into the reaction vessel by paraldehyde, the ratio of paraldehyde being so adjusted within the above limits that the reaction temperature remains within the limits of 280 DEG and 300 DEG C. Suitably, a mixture of acetaldehyde and formaldehyde is passed into the reaction vessel which may be a tube and paraldehyde is introduced at one or more points in the vessel. The positive heat production of the reaction is reduced by the heat required to depolymerize the paraldehyde to acetaldehyde, thereby facilitating temperature control. In an example, equimolecular proportions of 30 per cent aqueous formaldehyde and mixtures of acetaldehyde and paraldehyde containing 25, 60 and 80 per cent respectively of paraldehyde were preheated to 280 DEG C. and passed over a sodium silicate-silica gel catalyst at 280-300 DEG C., the temperature rise being 10 DEG , 0-3 DEG and 0 DEG C. respectively, whereas in the absence of paraldehyde it is 20-40 DEG C. The reaction mixture comprises acrolein, water, acetaldehyde, paraldehyde and crotonaldehyde and it may be worked up as described in Specification 568,529 using, for example, xylene or isopropyl benzene as the extracting agent, whereby an acrolein, crotonaldehyde and paraldehyde extract is obtained from which acrolein is recovered by distillation. Alternatively, acetaldehyde and acrolein may be distilled off from the reaction mixture and the residual mixture then distilled under reduced pressure or extracted with a hydrocarbon solvent to recover crotonaldehyde and paraldehyde. Specification 497,757 also is referred to. The Provisional Specification states that part of the acetaldehyde may be replaced by paraldehyde and that paraldehyde itself may be used as the extracting solvent in the recovery stage.
GB1852643A 1943-11-08 Improvements in or relating to the production of acrolein Expired GB600454A (en)

Publications (1)

Publication Number Publication Date
GB600454A true GB600454A (en) 1948-04-09

Family

ID=1733985

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1852643A Expired GB600454A (en) 1943-11-08 Improvements in or relating to the production of acrolein

Country Status (1)

Country Link
GB (1) GB600454A (en)

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