EP3426645A4 - Herstellungsausrüstung zur herstellung von caprolacton - Google Patents

Herstellungsausrüstung zur herstellung von caprolacton Download PDF

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Publication number
EP3426645A4
EP3426645A4 EP17763648.7A EP17763648A EP3426645A4 EP 3426645 A4 EP3426645 A4 EP 3426645A4 EP 17763648 A EP17763648 A EP 17763648A EP 3426645 A4 EP3426645 A4 EP 3426645A4
Authority
EP
European Patent Office
Prior art keywords
production
caprolactone
equipment
production equipment
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
EP17763648.7A
Other languages
English (en)
French (fr)
Other versions
EP3426645A1 (de
Inventor
William John MAYO
Neil David EDWARDSON
Antony ORRELL
Jeremy Charles HAZLEHURST
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.)
Ingevity UK Ltd
Original Assignee
Perstorp AB
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 Perstorp AB filed Critical Perstorp AB
Publication of EP3426645A1 publication Critical patent/EP3426645A1/de
Publication of EP3426645A4 publication Critical patent/EP3426645A4/de
Pending legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2415—Tubular reactors
    • B01J19/242—Tubular reactors in series
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18—Stationary reactors having moving elements inside
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D313/00—Heterocyclic compounds containing rings of more than six members having one oxygen atom as the only ring hetero atom
    • C07D313/02—Seven-membered rings
    • C07D313/04—Seven-membered rings not condensed with other rings
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2415—Tubular reactors
    • B01J19/243—Tubular reactors spirally, concentrically or zigzag wound
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002—Chemical plants
    • B01J2219/00004—Scale aspects
    • B01J2219/00006—Large-scale industrial plants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002—Chemical plants
    • B01J2219/00027—Process aspects
    • B01J2219/0004—Processes in series
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
    • B01J2219/00101—Reflux columns
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00105—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2219/0011—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
EP17763648.7A 2016-03-09 2017-03-03 Herstellungsausrüstung zur herstellung von caprolacton Pending EP3426645A4 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB1604114.7A GB2548138A (en) 2016-03-09 2016-03-09 Production equipment (II) for production of a caprolactone
PCT/SE2017/000018 WO2017155441A1 (en) 2016-03-09 2017-03-03 Production equipment for production of caprolactone

Publications (2)

Publication Number Publication Date
EP3426645A1 EP3426645A1 (de) 2019-01-16
EP3426645A4 true EP3426645A4 (de) 2019-08-14

Family

ID=55859280

Family Applications (1)

Application Number Title Priority Date Filing Date
EP17763648.7A Pending EP3426645A4 (de) 2016-03-09 2017-03-03 Herstellungsausrüstung zur herstellung von caprolacton

Country Status (3)

Country Link
EP (1) EP3426645A4 (de)
GB (1) GB2548138A (de)
WO (1) WO2017155441A1 (de)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11208394B2 (en) 2018-09-17 2021-12-28 Regents Of The University Of Minnesota Chemical process to manufacture branched-caprolactone
CN109705083A (zh) * 2019-01-29 2019-05-03 安徽华业香料合肥有限公司 一种ε-癸内酯香料的合成方法
CN109748900A (zh) * 2019-01-29 2019-05-14 安徽华业香料合肥有限公司 一种ε-癸内酯合成香料的生产方法
DE102019103123A1 (de) 2019-02-08 2020-08-13 Tesa Se Thermisch erweichbares Klebeband und Verfahren zum Ummanteln von langgestrecktem Gut insbesondere Leitungen
DE102019103120A1 (de) 2019-02-08 2020-08-13 Tesa Se UV-härtbares Klebeband und Verfahren zum Ummanteln von langgestrecktem Gut insbesondere Leitungen
DE102019103122A1 (de) 2019-02-08 2020-08-13 Tesa Se Mit Feuchtigkeit härtbares Klebeband und Verfahren zum Ummanteln von langgestrecktem Gut insbesondere Leitungen

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3625975A (en) * 1966-09-30 1971-12-07 Laporte Chemical Lactones by oxidation process
US3766212A (en) * 1970-08-01 1973-10-16 Bayer Ag Process for the preparation of epsilon-caprolactone
JPS5742684A (en) * 1980-08-28 1982-03-10 Daicel Chem Ind Ltd Preparation of epsilon-caprolactone
US4341709A (en) * 1979-05-19 1982-07-27 Bayer Aktiengesellschaft Preparation of ε-caprolactone
US4994583A (en) * 1982-01-15 1991-02-19 Produits Chimiques Uging Kuhlmann Process for the preparation of epsilon-caprolactone
EP1004576A1 (de) * 1998-11-23 2000-05-31 SOLVAY (Société Anonyme) Verfahren zur Herstellung von Peressigsäure
US20060173209A1 (en) * 2004-07-28 2006-08-03 Peragen Systems Inc. Continuous Process For On Site And On Demand Production Of Aqueous Peracetic Acid
US20080275132A1 (en) * 2006-10-18 2008-11-06 Mcsherry David D Apparatus and method for making a peroxycarboxylic acid
CN103539770A (zh) * 2013-10-08 2014-01-29 常州大学 一种制备ε-己内酯的连续反应工艺方法及微通道反应装备

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2519300C3 (de) * 1975-04-30 1979-06-13 Bayer Ag, 5090 Leverkusen Verfahren zur Herstellung von Perpropionsäurelösungen unter explosionssicheren Bedingungen
DE2934659A1 (de) * 1979-08-28 1981-03-19 Bayer Ag, 5090 Leverkusen Verfahren zur herstellung von sehr reinem epsilon -caprolacton
FR2500453A1 (fr) * 1981-02-20 1982-08-27 Ugine Kuhlmann Procede d'obtention de l'epsilon-caprolactone
JPH0798816B2 (ja) * 1990-04-25 1995-10-25 宇部興産株式会社 ε―カプロラクトンの製造法
CN102584775B (zh) * 2011-01-12 2015-04-22 中国石油化工集团公司 制备ε-己内酯的方法
CN102584776A (zh) * 2011-01-12 2012-07-18 中国石油化工集团公司 一种制备ε-己内酯的方法
CN103570667B (zh) * 2012-08-09 2015-01-21 中国石油化工股份有限公司 一种连续制备ε一己内酯的方法
CN104003972A (zh) * 2014-04-28 2014-08-27 安徽红太阳新材料有限公司 一种制备己内酯的方法
CN104119309B (zh) * 2014-07-24 2016-03-09 江苏红太阳新材料有限公司 一种环境友好型催化剂用于合成ε-己内酯的方法
CN105646433A (zh) * 2014-11-11 2016-06-08 中国石油化工股份有限公司 一种连续制备高纯ε－己内酯的工艺
CN104370873A (zh) * 2014-11-21 2015-02-25 南京工业大学 一种由环己酮催化氧化制备己内酯的方法

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3625975A (en) * 1966-09-30 1971-12-07 Laporte Chemical Lactones by oxidation process
US3766212A (en) * 1970-08-01 1973-10-16 Bayer Ag Process for the preparation of epsilon-caprolactone
US4341709A (en) * 1979-05-19 1982-07-27 Bayer Aktiengesellschaft Preparation of ε-caprolactone
JPS5742684A (en) * 1980-08-28 1982-03-10 Daicel Chem Ind Ltd Preparation of epsilon-caprolactone
US4994583A (en) * 1982-01-15 1991-02-19 Produits Chimiques Uging Kuhlmann Process for the preparation of epsilon-caprolactone
EP1004576A1 (de) * 1998-11-23 2000-05-31 SOLVAY (Société Anonyme) Verfahren zur Herstellung von Peressigsäure
US20060173209A1 (en) * 2004-07-28 2006-08-03 Peragen Systems Inc. Continuous Process For On Site And On Demand Production Of Aqueous Peracetic Acid
US20080275132A1 (en) * 2006-10-18 2008-11-06 Mcsherry David D Apparatus and method for making a peroxycarboxylic acid
CN103539770A (zh) * 2013-10-08 2014-01-29 常州大学 一种制备ε-己内酯的连续反应工艺方法及微通道反应装备

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of WO2017155441A1 *

Also Published As

Publication number Publication date
GB201604114D0 (en) 2016-04-20
EP3426645A1 (de) 2019-01-16
WO2017155441A1 (en) 2017-09-14
GB2548138A (en) 2017-09-13

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