EP3107885A1 - Procede de production d'acide acrylique bio-source - Google Patents

Procede de production d'acide acrylique bio-source

Info

Publication number
EP3107885A1
EP3107885A1 EP15709257.8A EP15709257A EP3107885A1 EP 3107885 A1 EP3107885 A1 EP 3107885A1 EP 15709257 A EP15709257 A EP 15709257A EP 3107885 A1 EP3107885 A1 EP 3107885A1
Authority
EP
European Patent Office
Prior art keywords
acrylic acid
column
dehydration
stream
glycerol
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.)
Withdrawn
Application number
EP15709257.8A
Other languages
German (de)
English (en)
French (fr)
Inventor
Jean-François Devaux
Michel Fauconet
Sandeep Jain
Stephen TLATLIK
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.)
Arkema France SA
Original Assignee
Arkema France SA
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 Arkema France SA filed Critical Arkema France SA
Publication of EP3107885A1 publication Critical patent/EP3107885A1/fr
Withdrawn legal-status Critical Current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
    • C07C45/51Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition
    • C07C45/52Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition by dehydration and rearrangement involving two hydroxy groups in the same molecule
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C47/00Compounds having —CHO groups
    • C07C47/20Unsaturated compounds having —CHO groups bound to acyclic carbon atoms
    • C07C47/21Unsaturated compounds having —CHO groups bound to acyclic carbon atoms with only carbon-to-carbon double bonds as unsaturation
    • C07C47/22Acryaldehyde; Methacryaldehyde
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/25Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring
    • C07C51/252Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring of propene, butenes, acrolein or methacrolein
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/43Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/43Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
    • C07C51/44Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/487Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C57/00Unsaturated compounds having carboxyl groups bound to acyclic carbon atoms
    • C07C57/02Unsaturated compounds having carboxyl groups bound to acyclic carbon atoms with only carbon-to-carbon double bonds as unsaturation
    • C07C57/03Monocarboxylic acids
    • C07C57/04Acrylic acid; Methacrylic acid
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/08Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/48Separation; Purification; Stabilisation; Use of additives
    • C07C67/52Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation
    • C07C67/54Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/48Separation; Purification; Stabilisation; Use of additives
    • C07C67/58Separation; Purification; Stabilisation; Use of additives by liquid-liquid treatment
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • C07C69/52Esters of acyclic unsaturated carboxylic acids having the esterified carboxyl group bound to an acyclic carbon atom
    • C07C69/533Monocarboxylic acid esters having only one carbon-to-carbon double bond
    • C07C69/54Acrylic acid esters; Methacrylic acid esters
    • 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
    • Y02P20/582Recycling of unreacted starting or intermediate materials

Definitions

  • the first step in the manufacture of acrylic acid from glycerol results in the same intermediate compound as the conventional manufacturing process from propylene, namely acrolein, according to the reaction:
  • a heat exchanger which may be a reboiler or cooler, before being returned to the dewatering column; a part of the dehydration column foot stream is brought into direct contact with the gaseous reaction mixture previously cooled or otherwise and the resulting stream is sent to step i); at least a portion of the overhead stream of the dehydration column is sent to the dehydration step of glycerol;
  • step b) said method being characterized in that the conditions of the separation of step b) are adapted to achieve the water / acrylic acid mass ratio desired in step c).
  • the recovery / purification process without external organic solvent is applied to a gaseous reaction mixture comprising a water / acrylic acid mass ratio of less than 1.6, preferably of between 0.3 and 1.5, and preferably between 0.3 and 1.2 and more particularly between 0.4 and 1.1.
  • any type of cooling apparatus known to those skilled in the art can be used, such as tubular exchangers, plate, finned, or any type of equipment for contacting a hot gas phase with a liquid phase cold, either by direct contact of the hot gas stream with the dispersed cold liquid flow, for example by means of nozzles, or by contact through trays or packings of all types known to those skilled in the art, etc.
  • most of the water present in the gaseous reaction mixture comprising acrylic acid is removed during step i) without there being excessive loss of acrylic acid in the reaction mixture. head flow.
  • the water content in the foot flow of the dewatering column is generally less than 10%, preferably less than 7%.
  • the acetic acid present in the gaseous reaction stream is extracted mainly in gaseous form, in the head flow of the dehydration column. It is not necessary to vaporize this flow, already in the gaseous state, before subjecting it to oxidation treatment in an oxidizer, which results in a reduction of the energy to be supplied. Furthermore, the energy produced during the exothermic oxidation of the mixture rich in acetic acid, which has a high thermal level, can be advantageously reused in the process, for example to vaporize the glycerol prior to the dehydration reaction in the first one.
  • the dehydration column generally comprises from 5 to 50 theoretical plates, preferably from 20 to 30 theoretical plates; the purification column generally comprises from 5 to 30 theoretical plates, preferably from 8 to 20 theoretical plates.
  • the choice of columns and the choice of ancillary equipment such as heat exchangers, condensers, pumps, fluid inlet and outlet will be easily determined according to considerations known to those skilled in the art.
  • the dehydration reaction of glycerol is generally carried out on acidic solid catalysts.
  • Suitable catalysts are homogeneous or multiphase materials which are insoluble in the reaction medium and which have a Hammett acidity, denoted H 0 of less than +2.
  • H 0 Hammett acidity
  • Example 1 purification of a gaseous reaction mixture of acrylic acid with a mass ratio water / acrylic acid of 1.09.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
EP15709257.8A 2014-02-19 2015-02-16 Procede de production d'acide acrylique bio-source Withdrawn EP3107885A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR1451315A FR3017617B1 (fr) 2014-02-19 2014-02-19 Procede de production d'acide acrylique bio-source
PCT/FR2015/050371 WO2015124856A1 (fr) 2014-02-19 2015-02-16 Procede de production d'acide acrylique bio-source

Publications (1)

Publication Number Publication Date
EP3107885A1 true EP3107885A1 (fr) 2016-12-28

Family

ID=52649052

Family Applications (1)

Application Number Title Priority Date Filing Date
EP15709257.8A Withdrawn EP3107885A1 (fr) 2014-02-19 2015-02-16 Procede de production d'acide acrylique bio-source

Country Status (7)

Country Link
US (1) US10029975B2 (enExample)
EP (1) EP3107885A1 (enExample)
JP (1) JP2017509604A (enExample)
KR (1) KR20160124194A (enExample)
CN (1) CN105980343B (enExample)
FR (1) FR3017617B1 (enExample)
WO (1) WO2015124856A1 (enExample)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR3060000B1 (fr) * 2016-12-08 2020-05-01 Arkema France Procede pour eviter le depot de polymeres dans un procede de purification d'acide (meth)acrylique.
US11773215B2 (en) * 2018-04-06 2023-10-03 Novomer, Inc. Polypropiolactone films, and methods of producing thereof
FR3162750A1 (fr) * 2024-05-30 2025-12-05 Arkema France Procede de purification d’acide (meth)acrylique

Family Cites Families (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4238493C1 (de) 1992-11-14 1994-04-21 Degussa Verfahren zur Herstellung von Acrolein und dessen Verwendung
DE19740253A1 (de) * 1997-09-12 1999-03-18 Basf Ag Verfahren zur fraktionierten Kondensation eines heißen Gasgemisches mit einem hohen Anteil nicht kondensierbarer Komponenten
DE19848208A1 (de) 1998-10-20 2000-04-27 Deg Engineering Gmbh Reaktor für die katalytische Umsetzung von Reaktionsmedien, insbesondere von gasförmigen Reaktionsmedien
DE50003359D1 (de) 1999-03-06 2003-09-25 Basf Ag Verfahren zur herstellung von acrylsäure
DE10019381B4 (de) 2000-04-19 2006-05-18 Daun, Klaus-Dieter, Dipl.-Ing. Reaktor für die katalytische Umsetzung von Reaktionsmedien, insbesondere von gasförmigen Reaktionsmedien
JP3957298B2 (ja) 2003-06-05 2007-08-15 株式会社日本触媒 アクリル酸の製造方法
US7268254B2 (en) 2003-07-24 2007-09-11 Basf Aktiengesellschaft Preparation of (meth)acrolein and/or (meth)acrylic acid by heterogeneously catalyzed partial oxidation of C3 and/or C4 precursor compounds in a reactor having thermoplate modules
JP5006507B2 (ja) 2004-01-30 2012-08-22 株式会社日本触媒 アクリル酸の製造方法
FR2882052B1 (fr) 2005-02-15 2007-03-23 Arkema Sa Procede de deshydratation du glycerol en acroleine
FR2882053B1 (fr) 2005-02-15 2007-03-23 Arkema Sa Procede de deshydratation du glycerol en acrolene
TWI522092B (zh) 2005-02-28 2016-02-21 贏創德固賽有限責任公司 丙烯酸和基於可再生原料之吸水聚合物結構及二者之製備方法
FR2884818B1 (fr) 2005-04-25 2007-07-13 Arkema Sa Procede de preparation d'acide acrylique a partir de glycerol
US20090068440A1 (en) 2005-06-20 2009-03-12 Gunther Bub Production of acrolein, acrylic acid and water-absorbent polymer structures made from glycerine
US7495505B2 (en) 2006-07-18 2009-02-24 Faraday Technology Corp. Low supply voltage band-gap reference circuit and negative temperature coefficient current generation unit thereof and method for supplying band-gap reference current
US8242308B2 (en) * 2006-09-15 2012-08-14 Arkema Inc. Process for producing acrylic acid
JP2008115103A (ja) 2006-11-02 2008-05-22 Nippon Shokubai Co Ltd アクリル酸の製造方法、アクリル酸製造用装置、およびアクリル酸製造用組成物
FR2909999B1 (fr) 2006-12-19 2009-04-03 Arkema France Procede de preparation d'acide acrylique a partir de glycerol
BRPI0704952A2 (pt) 2007-04-04 2008-11-18 Rohm & Haas mÉtodo para a purificaÇço de glicerol
WO2009127889A1 (en) 2008-04-16 2009-10-22 Arkema France Process for manufacturing acrolein from glycerol
FR2935971B1 (fr) 2008-09-16 2010-11-19 Arkema France Acide bio-acrylique de grade polymere et son procede de fabrication a partir de glycerol.
EP2179981A1 (en) 2008-10-24 2010-04-28 Arkema France Process for manufacturing acrolein from glycerol
EP2371801A4 (en) 2008-12-26 2012-10-17 Nippon Catalytic Chem Ind PROCESS FOR THE PRODUCTION OF ACRYLIC ACID
JP5583666B2 (ja) 2009-06-01 2014-09-03 株式会社日本触媒 (メタ)アクリル酸の晶析方法および製品(メタ)アクリル酸の重合防止剤含有量の調整方法
FR2948365B1 (fr) 2009-07-22 2011-09-09 Arkema France Procede de fabrication d'acide acrylique bio-ressource a partir de glycerol
FR2948366B1 (fr) 2009-07-22 2012-08-17 Arkema France Procede de fabrication d'acide acrylique bio-ressource a partir de glycerol
SG179188A1 (en) 2009-09-18 2012-04-27 Nippon Kayaku Kk Catalyst and process for preparing acrolein and/or acrylic acid by dehydration reaction of glycerin
FR2953829B1 (fr) * 2009-12-14 2011-12-09 Arkema France Procede de fabrication d'acroleine et/ou d'acide acrylique a partir de glycerol
FR2957594B1 (fr) 2010-03-18 2013-04-26 Arkema France Procede de fabrication d'acide acrylique bio-ressource de grade polymere a partir de glycerol
WO2012101471A1 (en) 2011-01-28 2012-08-02 Arkema France Improved process for manufacturing acrolein/acrylic acid

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
None *
See also references of WO2015124856A1 *

Also Published As

Publication number Publication date
KR20160124194A (ko) 2016-10-26
CN105980343A (zh) 2016-09-28
WO2015124856A1 (fr) 2015-08-27
US10029975B2 (en) 2018-07-24
FR3017617A1 (fr) 2015-08-21
US20170166507A1 (en) 2017-06-15
FR3017617B1 (fr) 2016-02-12
JP2017509604A (ja) 2017-04-06
CN105980343B (zh) 2018-05-18

Similar Documents

Publication Publication Date Title
EP2300411B1 (fr) Procede de fabrication d'acide propionique bio-ressource a partir de glycerol
EP2097365B1 (fr) Procede de preparation d'acide acrylique a partir de glycerol
EP2326615B1 (fr) Procede de fabrication d'acide acrylique bio-ressource de grade polymere a partir de glycerol
EP2456743B1 (fr) Procede de fabrication d'acide acrylique bio-ressource a partir de glycerol
EP2513027B1 (fr) Procede de fabrication d'acroleine et/ou d'acide acrylique a partir de glycerol
WO2007090991A2 (fr) Procede de preparation d'acide acrylique
EP2513026B1 (fr) Procede de fabrication d'acroleine et/ou d'acide acrylique a partir de glycerol
EP3606903B1 (fr) Procede de purification d'acide (meth)acrylique incluant une colonne de distillation a paroi separatrice.
EP2547643A1 (fr) Procede de fabrication d'acide acrylique bio-ressource de grade polymere a partir de glycerol
EP2456746A1 (fr) Procede de fabrication d'acide acrylique bio-ressource a partir de glycerol
EP3107885A1 (fr) Procede de production d'acide acrylique bio-source
FR2957918A1 (fr) Procede d'obtention d'un ester d'acide carboxylique
TWI574943B (zh) 製備甲基丙烯酸和甲基丙烯酸酯類之方法
FR2955859A1 (fr) Procede de preparation d'un ester d'acide carboxylique
EP4132898B1 (fr) Procede de purification d'acide (meth)acrylique
EP4392399A1 (fr) Procede perfectionne de fabrication d'acrylate de butyle de purete elevee

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

17P Request for examination filed

Effective date: 20160610

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

DAX Request for extension of the european patent (deleted)
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS

17Q First examination report despatched

Effective date: 20170925

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20180914