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
Links
- 238000006068 polycondensation reaction Methods 0.000 abstract 5
- 239000003054 catalyst Substances 0.000 abstract 3
- 230000032050 esterification Effects 0.000 abstract 3
- 238000005886 esterification reaction Methods 0.000 abstract 3
- 230000005494 condensation Effects 0.000 abstract 2
- 238000009833 condensation Methods 0.000 abstract 2
- 239000000178 monomer Substances 0.000 abstract 2
- XKZQKPRCPNGNFR-UHFFFAOYSA-N 2-(3-hydroxyphenyl)phenol Chemical compound OC1=CC=CC(C=2C(=CC=CC=2)O)=C1 XKZQKPRCPNGNFR-UHFFFAOYSA-N 0.000 abstract 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical group OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 abstract 1
- ABLZXFCXXLZCGV-UHFFFAOYSA-N Phosphorous acid Chemical group OP(O)=O ABLZXFCXXLZCGV-UHFFFAOYSA-N 0.000 abstract 1
- 239000004952 Polyamide Substances 0.000 abstract 1
- 239000000654 additive Substances 0.000 abstract 1
- 125000003277 amino group Chemical group 0.000 abstract 1
- 150000008064 anhydrides Chemical group 0.000 abstract 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 abstract 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 abstract 1
- 150000001875 compounds Chemical class 0.000 abstract 1
- 150000004985 diamines Chemical class 0.000 abstract 1
- ZFTFAPZRGNKQPU-UHFFFAOYSA-N dicarbonic acid Chemical compound OC(=O)OC(O)=O ZFTFAPZRGNKQPU-UHFFFAOYSA-N 0.000 abstract 1
- 150000002170 ethers Chemical class 0.000 abstract 1
- 125000000524 functional group Chemical group 0.000 abstract 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- ACVYVLVWPXVTIT-UHFFFAOYSA-M phosphinate Chemical group [O-][PH2]=O ACVYVLVWPXVTIT-UHFFFAOYSA-M 0.000 abstract 1
- -1 phosphino groups Chemical group 0.000 abstract 1
- 125000001476 phosphono group Chemical group [H]OP(*)(=O)O[H] 0.000 abstract 1
- 229920001643 poly(ether ketone) Polymers 0.000 abstract 1
- 229920002492 poly(sulfone) Polymers 0.000 abstract 1
- 229920002647 polyamide Polymers 0.000 abstract 1
- 229920001230 polyarylate Polymers 0.000 abstract 1
- 229920000412 polyarylene Polymers 0.000 abstract 1
- 125000005373 siloxane group Chemical group [SiH2](O*)* 0.000 abstract 1
- 125000001273 sulfonato group Chemical group [O-]S(*)(=O)=O 0.000 abstract 1
- 125000000472 sulfonyl group Chemical group *S(*)(=O)=O 0.000 abstract 1
Classifications
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- 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
- B01J19/20—Stationary reactors having moving elements inside in the form of helices, e.g. screw reactors
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/78—Preparation processes
- C08G63/785—Preparation processes characterised by the apparatus used
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G64/00—Macromolecular compounds obtained by reactions forming a carbonic ester link in the main chain of the macromolecule
- C08G64/20—General preparatory processes
- C08G64/205—General preparatory processes characterised by the apparatus used
-
- 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
- B01J2219/00761—Details of the reactor
- B01J2219/00763—Baffles
- B01J2219/00765—Baffles attached to the reactor wall
- B01J2219/00777—Baffles attached to the reactor wall horizontal
-
- 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
- B01J2219/00761—Details of the reactor
- B01J2219/00763—Baffles
- B01J2219/00779—Baffles 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.
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)
| 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)
| 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 |
-
2004
- 2004-07-17 DE DE102004034708A patent/DE102004034708B4/en not_active Withdrawn - After Issue
-
2005
- 2005-07-02 WO PCT/EP2005/007171 patent/WO2006007966A1/en not_active Ceased
- 2005-07-02 AT AT05772235T patent/ATE384576T1/en not_active IP Right Cessation
- 2005-07-02 KR KR1020077002341A patent/KR20070032800A/en not_active Withdrawn
- 2005-07-02 US US11/572,241 patent/US20080051529A1/en not_active Abandoned
- 2005-07-02 JP JP2007520707A patent/JP2008506795A/en not_active Withdrawn
- 2005-07-02 DE DE502005002681T patent/DE502005002681D1/en not_active Expired - Fee Related
- 2005-07-02 CN CNA2005800241488A patent/CN1988951A/en active Pending
- 2005-07-02 EP EP05772235A patent/EP1768775B1/en not_active Expired - Lifetime
- 2005-07-02 EA EA200700039A patent/EA200700039A1/en unknown
-
2007
- 2007-01-15 IL IL180716A patent/IL180716A0/en unknown
- 2007-01-31 IN IN207CH2007 patent/IN2007CH00207A/en unknown
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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