GB670445A - Recovery of by-products in the manufacture of phenol - Google Patents

Recovery of by-products in the manufacture of phenol

Info

Publication number
GB670445A
GB670445A GB15221/49A GB1522149A GB670445A GB 670445 A GB670445 A GB 670445A GB 15221/49 A GB15221/49 A GB 15221/49A GB 1522149 A GB1522149 A GB 1522149A GB 670445 A GB670445 A GB 670445A
Authority
GB
United Kingdom
Prior art keywords
phenol
cumylphenol
alkali
washed
products
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
GB15221/49A
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
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 Distillers Co Yeast Ltd, Distillers Co Ltd filed Critical Distillers Co Yeast Ltd
Priority to GB15221/49A priority Critical patent/GB670445A/en
Publication of GB670445A publication Critical patent/GB670445A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/005Processes comprising at least two steps in series
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C37/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
    • C07C37/68Purification; separation; Use of additives, e.g. for stabilisation
    • C07C37/70Purification; separation; Use of additives, e.g. for stabilisation by physical treatment
    • C07C37/74Purification; separation; Use of additives, e.g. for stabilisation by physical treatment by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/04Purification; Separation; Use of additives by distillation
    • 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)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

In phenol production by acidic decomposition of isopropylbenzene peroxides, the reaction mixture is fractionally distilled under non-acid conditions, i.e. pH not below 5. Thus the mixture is washed with water to remove the acid catalyst, followed by small amounts of alkali to remove organic acidic by-products and to produce the desired pH change without removing appreciable amounts of phenol. Small amounts of phenol and acetone may be recovered from the wash water. Preferably also the peroxides are alkali-washed before contact with the acidic decomposition agent. Fractional distillation of the washed decomposition products yields successively isopropylbenzene, a - methylstyrene, phenol, acetophenone and cumylphenol, the last two preferably under reduced pressure. Alternatively, after the first- and second-named have passed over, the phenol and acetophenone are removed by steam distillation and the cumylphenol extracted from the residue with alkali. The cumylphenol may then be treated as in Specification 670,444 to increase the overall yield of phenol. An example is given of the process.
GB15221/49A 1949-06-08 1949-06-08 Recovery of by-products in the manufacture of phenol Expired GB670445A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB15221/49A GB670445A (en) 1949-06-08 1949-06-08 Recovery of by-products in the manufacture of phenol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB15221/49A GB670445A (en) 1949-06-08 1949-06-08 Recovery of by-products in the manufacture of phenol

Publications (1)

Publication Number Publication Date
GB670445A true GB670445A (en) 1952-04-16

Family

ID=10055180

Family Applications (1)

Application Number Title Priority Date Filing Date
GB15221/49A Expired GB670445A (en) 1949-06-08 1949-06-08 Recovery of by-products in the manufacture of phenol

Country Status (1)

Country Link
GB (1) GB670445A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1025891B (en) * 1953-09-02 1958-03-13 Distillers Co Yeast Ltd Process for the production of phenol or cresols
DE1128859B (en) * 1957-07-31 1962-05-03 Phenolchemie Ges Mit Beschraen Process for the continuous neutralization of cleavage mixtures which have been obtained by cleaving alkyl aromatic hydroperoxides in the presence of acids
WO2007119849A1 (en) 2006-04-17 2007-10-25 Asahi Kasei Chemicals Corporation METHOD FOR PURIFYING α-METHYLSTYRENE, AND HEAT-RESISTANT STYRENE COPOLYMER USING THE α-METHYLSTYRENE
CN106905103A (en) * 2017-04-06 2017-06-30 山东建筑大学 α-methylstyrene production technology is reclaimed in a kind of phenol raffinate

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1025891B (en) * 1953-09-02 1958-03-13 Distillers Co Yeast Ltd Process for the production of phenol or cresols
DE1128859B (en) * 1957-07-31 1962-05-03 Phenolchemie Ges Mit Beschraen Process for the continuous neutralization of cleavage mixtures which have been obtained by cleaving alkyl aromatic hydroperoxides in the presence of acids
WO2007119849A1 (en) 2006-04-17 2007-10-25 Asahi Kasei Chemicals Corporation METHOD FOR PURIFYING α-METHYLSTYRENE, AND HEAT-RESISTANT STYRENE COPOLYMER USING THE α-METHYLSTYRENE
EP2011807A1 (en) * 2006-04-17 2009-01-07 Asahi Kasei Chemicals Corporation Method for purifying -methylstyrene, and heat-resistant styrene copolymer using the -methylstyrene
EP2011807A4 (en) * 2006-04-17 2013-10-02 Asahi Kasei Chemicals Corp Method for purifying -methylstyrene, and heat-resistant styrene copolymer using the -methylstyrene
EP2743246A1 (en) * 2006-04-17 2014-06-18 Asahi Kasei Chemicals Corporation Alpha-Metylstyrene-based copolymer
CN106905103A (en) * 2017-04-06 2017-06-30 山东建筑大学 α-methylstyrene production technology is reclaimed in a kind of phenol raffinate

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