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IN2007CH00207A - - Google Patents

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Publication number
IN2007CH00207A
IN2007CH00207A IN207CH2007A IN2007CH00207A IN 2007CH00207 A IN2007CH00207 A IN 2007CH00207A IN 207CH2007 A IN207CH2007 A IN 207CH2007A IN 2007CH00207 A IN2007CH00207 A IN 2007CH00207A
Authority
IN
India
Prior art keywords
groups
reactor
polycondensation
reesterification
reactors
Prior art date
Application number
Inventor
Rudolf Kaempf
Original Assignee
Lurgi Zimmer Gmbh
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 Lurgi Zimmer Gmbh filed Critical Lurgi Zimmer Gmbh
Publication of IN2007CH00207A publication Critical patent/IN2007CH00207A/en
Priority to US12/021,971 priority Critical patent/US9223629B2/en
Priority to US14/853,415 priority patent/US20160004568A1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • B01J19/20Stationary reactors having moving elements inside in the form of helices, e.g. screw reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/78Preparation processes
    • C08G63/785Preparation processes characterised by the apparatus used
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G64/00Macromolecular compounds obtained by reactions forming a carbonic ester link in the main chain of the macromolecule
    • C08G64/20General preparatory processes
    • C08G64/205General preparatory processes characterised by the apparatus used
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002Chemical plants
    • B01J2219/00004Scale aspects
    • B01J2219/00006Large-scale industrial plants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00761Details of the reactor
    • B01J2219/00763Baffles
    • B01J2219/00765Baffles attached to the reactor wall
    • B01J2219/00777Baffles attached to the reactor wall horizontal
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00761Details of the reactor
    • B01J2219/00763Baffles
    • B01J2219/00779Baffles attached to the stirring means

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)
  • Polyamides (AREA)

Abstract

Disclosed are a method and a device for batchwise production of high-molecular polyphosphonates, polysulfones, polyarylates, polyamides, polyarylene ethers, or polyether ketones by melt-condensing a monomer compound carrying hydroxyl groups, carboxyl groups, anhydride groups, phosphoric acid groups, phosphono groups, phosphonate groups, phosphino groups, phosphinate groups, carbonyl groups, sulfonyl groups, sulfonate groups, siloxane groups or amino groups on its own or along with at least one diphenol, dialcohol, diamine, or a dicarbonate component. According to the invention, a) esterification or reesterification and precondensation are performed in a batchwise operated first reactor ( 1 ) in the presence of an esterification catalyst or reesterification catalyst; b) polycondensation is then optionally performed in a batchwise operated intermediate reactor ( 6 ) by optionally adding one or several additional monomers, another catalyst, and additives until a predetermined polycondensation level or viscosity level has been attained; and finally (c) condensation is continued in a batchwise operated final reactor ( 12 ) until the desired polycondensation level or viscosity level has been reached; and d) branching molecules comprising more than two functional groups are optionally added prior to or during esterification or reesterification, prior to or during polycondensation optionally performed in the intermediate reactor, or prior to or during polycondensation performed in the final reactor. The dwell time in the reactors ranges between 5 minutes and 15 hours while the temperature is set to 180 to 300° C. in reactors ( 1 ) and ( 6 ) and to 240 to 400° C. in reactor ( 12 ), the pressure being continuously or gradually lowered from 2000 to 100 mbar in reactors ( 1 ) and ( 6 ) and to 100 to 0.01 mbar in reactor ( 12 ) by sucking off the vapors produced during condensation.
IN207CH2007 2004-07-17 2007-01-31 IN2007CH00207A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US12/021,971 US9223629B2 (en) 2007-01-31 2008-01-29 Data processing system and method
US14/853,415 US20160004568A1 (en) 2007-01-31 2015-09-14 Data processing system and method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102004034708A DE102004034708B4 (en) 2004-07-17 2004-07-17 Process for the batch production of polymers by melt condensation

Publications (1)

Publication Number Publication Date
IN2007CH00207A true IN2007CH00207A (en) 2007-08-24

Family

ID=35106816

Family Applications (1)

Application Number Title Priority Date Filing Date
IN207CH2007 IN2007CH00207A (en) 2004-07-17 2007-01-31

Country Status (11)

Country Link
US (1) US20080051529A1 (en)
EP (1) EP1768775B1 (en)
JP (1) JP2008506795A (en)
KR (1) KR20070032800A (en)
CN (1) CN1988951A (en)
AT (1) ATE384576T1 (en)
DE (2) DE102004034708B4 (en)
EA (1) EA200700039A1 (en)
IL (1) IL180716A0 (en)
IN (1) IN2007CH00207A (en)
WO (1) WO2006007966A1 (en)

Families Citing this family (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6906164B2 (en) 2000-12-07 2005-06-14 Eastman Chemical Company Polyester process using a pipe reactor
US20080139780A1 (en) * 2006-12-07 2008-06-12 Debruin Bruce Roger Polyester production system employing short residence time esterification
US7943094B2 (en) * 2006-12-07 2011-05-17 Grupo Petrotemex, S.A. De C.V. Polyester production system employing horizontally elongated esterification vessel
US7649109B2 (en) 2006-12-07 2010-01-19 Eastman Chemical Company Polyester production system employing recirculation of hot alcohol to esterification zone
US7863477B2 (en) 2007-03-08 2011-01-04 Eastman Chemical Company Polyester production system employing hot paste to esterification zone
US7892498B2 (en) 2007-03-08 2011-02-22 Eastman Chemical Company Polyester production system employing an unagitated esterification reactor
US7847053B2 (en) 2007-07-12 2010-12-07 Eastman Chemical Company Multi-level tubular reactor with oppositely extending segments
US7872090B2 (en) 2007-07-12 2011-01-18 Eastman Chemical Company Reactor system with optimized heating and phase separation
US7829653B2 (en) 2007-07-12 2010-11-09 Eastman Chemical Company Horizontal trayed reactor
US7858730B2 (en) 2007-07-12 2010-12-28 Eastman Chemical Company Multi-level tubular reactor with dual headers
US7868130B2 (en) 2007-07-12 2011-01-11 Eastman Chemical Company Multi-level tubular reactor with vertically spaced segments
US7842777B2 (en) 2007-07-12 2010-11-30 Eastman Chemical Company Sloped tubular reactor with divided flow
US7872089B2 (en) 2007-07-12 2011-01-18 Eastman Chemical Company Multi-level tubular reactor with internal tray
US7868129B2 (en) 2007-07-12 2011-01-11 Eastman Chemical Company Sloped tubular reactor with spaced sequential trays
US7834109B2 (en) * 2007-12-07 2010-11-16 Eastman Chemical Company System for producing low impurity polyester
US20110105716A1 (en) * 2008-05-22 2011-05-05 Bernhard Stuetzle Process and apparatus for preparing biopolymers
MY159885A (en) * 2008-08-14 2017-02-15 Basf Se Batch process for preparing polyamides
DE102013210180A1 (en) * 2013-05-31 2014-12-04 Aquafil Engineering Gmbh Process for working up a mixture obtained during polycondensation processes and a plant for carrying out the process
CN107189061B (en) * 2017-05-17 2019-07-23 东华大学 A kind of Halogen melt-drip resistant inflaming retarding nylon 6 resin and preparation method thereof
CN108299643A (en) * 2018-01-26 2018-07-20 五邑大学 Phosphor-containing flame-proof type engineering plastics polysulfones and its synthetic method
AT521534A2 (en) * 2018-07-03 2020-02-15 Next Generation Recyclingmaschinen Gmbh Process for producing a polycondensate melt from a primary material and a secondary material
CN113813866B (en) * 2020-06-19 2024-10-15 欧瑞康巴马格惠通(扬州)工程有限公司 Flexible production system of polyester product

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL272388A (en) * 1960-12-16
DE4403452A1 (en) * 1993-04-26 1994-10-27 Zimmer Ag Discontinuous catalytic process for the production of polyamide-6.6
US5306804A (en) * 1993-04-26 1994-04-26 Zimmer Aktiengesellschaft Discontinuous process for the production of a polyamide-6,6
DE4440741A1 (en) * 1994-11-15 1996-05-23 Zimmer Ag Vacuum generation process in polycarbonate production
JPH08283394A (en) * 1995-04-10 1996-10-29 Mitsui Petrochem Ind Ltd Method for producing polyethylene terephthalate
US6277947B1 (en) * 2000-04-21 2001-08-21 Shell Oil Company Process of producing polytrimethylene terephthalate (PTT)
DE10001477B4 (en) * 2000-01-15 2005-04-28 Zimmer Ag Discontinuous polycondensation process and stirring disk reactor for this
DE10318747B4 (en) * 2003-04-25 2006-04-20 Zimmer Ag Method for producing a vacuum in the production of polymers
DE10336164B4 (en) * 2003-08-07 2005-08-25 Zimmer Ag Process and device for the continuous production of polymers by melt condensation

Also Published As

Publication number Publication date
IL180716A0 (en) 2007-06-03
DE102004034708A1 (en) 2006-02-09
ATE384576T1 (en) 2008-02-15
KR20070032800A (en) 2007-03-22
CN1988951A (en) 2007-06-27
JP2008506795A (en) 2008-03-06
WO2006007966A1 (en) 2006-01-26
DE502005002681D1 (en) 2008-03-13
EP1768775A1 (en) 2007-04-04
EP1768775B1 (en) 2008-01-23
DE102004034708B4 (en) 2008-04-10
US20080051529A1 (en) 2008-02-28
EA200700039A1 (en) 2007-08-31

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