JPS5742684A - Preparation of epsilon-caprolactone - Google Patents

Preparation of epsilon-caprolactone

Info

Publication number
JPS5742684A
JPS5742684A JP11912380A JP11912380A JPS5742684A JP S5742684 A JPS5742684 A JP S5742684A JP 11912380 A JP11912380 A JP 11912380A JP 11912380 A JP11912380 A JP 11912380A JP S5742684 A JPS5742684 A JP S5742684A
Authority
JP
Japan
Prior art keywords
reaction mixture
boiling components
cyclohexanone
acid
column
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.)
Pending
Application number
JP11912380A
Other languages
Japanese (ja)
Inventor
Kazuhiko Nakano
Yutaka Ashikawa
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.)
Daicel Corp
Original Assignee
Daicel Corp
Daicel Chemical Industries 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 Daicel Corp, Daicel Chemical Industries Ltd filed Critical Daicel Corp
Priority to JP11912380A priority Critical patent/JPS5742684A/en
Publication of JPS5742684A publication Critical patent/JPS5742684A/en
Pending legal-status Critical Current

Links

Landscapes

  • Pyrane Compounds (AREA)

Abstract

PURPOSE: To obtain ε-caprolactone useful as a raw material of polymer, etc., in high yield, by separating and puritying the reaction mixture obtained by oxidizing cyclohexanone with an organic peracid using a specific distillation method, thereby preventing the polymerization loss during the oxidation and distillation steps.
CONSTITUTION: Cyclohexanone is oxidized with an organic peracid (e.g. peracetic acid, perpropionic acid, etc.), and low-boiling components (acetic acid, ethyl acetate, unreacted cyclohexanone, and peracetic acid) are distilled out from the reaction mixture. After the treatment, the reaction mixture is again distilled with an apparatus furnished with a one-pass thin-film evaporator to obtain the objective compound. For example, the reaction mixture is fed to a column 1 through the pipe 2 to distill off the low-boiling components, and the bottom residue is supplied to the distillation column 4 for removing high-boiling components and furnished with a single-pass thin-film evaporator 5. The by-product (e.g. polycaprolactone and adipic acid) is removed from the bottom of the evaporator 6 and the objective product is obtained from the top 7 of the column. The polymerization loss can be remarkably reduced by the combination of the proper selection of the reaction mixture based on the organic peracid process and the prevention of contact of the high- boiling components with the objective product utilizing the single-pass process.
COPYRIGHT: (C)1982,JPO&Japio
JP11912380A 1980-08-28 1980-08-28 Preparation of epsilon-caprolactone Pending JPS5742684A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11912380A JPS5742684A (en) 1980-08-28 1980-08-28 Preparation of epsilon-caprolactone

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11912380A JPS5742684A (en) 1980-08-28 1980-08-28 Preparation of epsilon-caprolactone

Publications (1)

Publication Number Publication Date
JPS5742684A true JPS5742684A (en) 1982-03-10

Family

ID=14753501

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11912380A Pending JPS5742684A (en) 1980-08-28 1980-08-28 Preparation of epsilon-caprolactone

Country Status (1)

Country Link
JP (1) JPS5742684A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6063938A (en) * 1996-07-29 2000-05-16 Mitsubishi Gas Chemical Company, Inc. Process for producing ε-caprolactone
JP2011042810A (en) * 2010-12-03 2011-03-03 Nippon Zeon Co Ltd Method for producing alkyl jasmonate with high epimer concentration
CN109789341A (en) * 2016-09-28 2019-05-21 佩什托普公司 Processing by caprolactone produce in the device and method of product stream that generate
EP3426645A4 (en) * 2016-03-09 2019-08-14 Perstorp AB Production equipment for production of caprolactone

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5218197A (en) * 1975-08-01 1977-02-10 Citizen Watch Co Ltd Drive circuit for electrochromism display

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5218197A (en) * 1975-08-01 1977-02-10 Citizen Watch Co Ltd Drive circuit for electrochromism display

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6063938A (en) * 1996-07-29 2000-05-16 Mitsubishi Gas Chemical Company, Inc. Process for producing ε-caprolactone
JP2011042810A (en) * 2010-12-03 2011-03-03 Nippon Zeon Co Ltd Method for producing alkyl jasmonate with high epimer concentration
EP3426645A4 (en) * 2016-03-09 2019-08-14 Perstorp AB Production equipment for production of caprolactone
CN109789341A (en) * 2016-09-28 2019-05-21 佩什托普公司 Processing by caprolactone produce in the device and method of product stream that generate

Similar Documents

Publication Publication Date Title
EP0551111B1 (en) Process for purifying acrylic acid to high purity in the production of acrylic acid
US4058555A (en) Process for the purification of mixed acids
MY118128A (en) The preparation of 1, 6-hexanediol and caprolactone
EP0061393B1 (en) Continuous process for the preparation of propylene oxide
JPS60115532A (en) Production of butadiene
DE3429391A1 (en) METHOD FOR PRODUCING ACRYLIC ACID
JPH05246941A (en) Method for purifying acrylic acid in high yield in production of acrylic acid
US3878057A (en) Plural stage distillation of a crude 3-methylmercaptopropionaldehyde feed in solution with a volatile weak acid and a less volatile strong acid
JPS5742684A (en) Preparation of epsilon-caprolactone
GB2063264A (en) Treatment of waste stream from adipic acid manufacture
JP4001861B2 (en) Method for removing formic acid from aqueous solution
JP3301245B2 (en) Method for recovering propylene oxide
EP0519139A1 (en) Process for the purification of glycidyl (meth)acrylate
ATE126222T1 (en) METHOD FOR PRODUCING TETRAHYDROFURAN AND ALPHA-BUTYROLACTONE.
JPH0987273A (en) Purification of epsilon-caprolactone
JPH0334945A (en) Removal of acidic impurities from feedstock containing tertiary butylperoxide
US3449219A (en) Process for fractionating propylene from propylene oxide in the presence of hydrocarbon flux
JP2003055303A (en) Method for producing 4-6c dicarboxylic acid esters from alkali waste fluid occurring in caprolactam production process
JP4204097B2 (en) Method for producing methyl methacrylate
JP3880128B2 (en) Acrylic acid recovery method
US4365080A (en) Production of dimethyl esters
JPS5829790B2 (en) Continuous production method of percarboxylic acid in organic solvent
JP4173572B2 (en) Method for purifying ε-caprolactone
WO1999014190A1 (en) Process for preparing equilibrium peroxy acid and process for producing lactone
JP4147354B2 (en) Process for producing ε-caprolactone