FR2387258A1 - Procede continu de preparation de poly(terephtalate d'ethylene) par esterification directe et polymerisation avec recuperation et recyclage de l'ethyleneglycol vaporise - Google Patents
Procede continu de preparation de poly(terephtalate d'ethylene) par esterification directe et polymerisation avec recuperation et recyclage de l'ethyleneglycol vaporiseInfo
- Publication number
- FR2387258A1 FR2387258A1 FR7810883A FR7810883A FR2387258A1 FR 2387258 A1 FR2387258 A1 FR 2387258A1 FR 7810883 A FR7810883 A FR 7810883A FR 7810883 A FR7810883 A FR 7810883A FR 2387258 A1 FR2387258 A1 FR 2387258A1
- Authority
- FR
- France
- Prior art keywords
- polymerization
- poly
- continuous process
- ethylene terephthalate
- direct esterification
- 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.)
- Granted
Links
Classifications
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Polyesters Or Polycarbonates (AREA)
Abstract
L'invention se rapporte au génie chimique. Elle concerne un procède continu d'estérification directe d'acide téréphtalique par de l'éthylèneglycol, suivi d'une polymérisation sous basse pression dans un appareil de prépolymérisation 30 et dans un appareil de polymérisation finale 46, dans lequel les vapeurs provenant des appareils de polymérisation sont condensées dans des condenseurs à pulverisation 52, 66 pour recueillir du glycol liquide que l'on recycle au réacteur d'estérification 24. Un fonctionnement efficace des condenseurs à des pressions de moins de 60 mm de Hg est obtenu par addition (en 70) d'éthylèneglycol pratiquement anhydre pour réduire la teneur en eau du condensat utilisé dans les pulverisateurs. Utilisation dans la production de poly(téréphtalate d'éthylène) filable à l'état fondu en fils textiles.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US05/787,605 US4110316A (en) | 1977-04-14 | 1977-04-14 | Improved process for preparing poly(ethylene terephthalate) |
Publications (2)
Publication Number | Publication Date |
---|---|
FR2387258A1 true FR2387258A1 (fr) | 1978-11-10 |
FR2387258B1 FR2387258B1 (fr) | 1985-05-17 |
Family
ID=25142009
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR7810883A Granted FR2387258A1 (fr) | 1977-04-14 | 1978-04-13 | Procede continu de preparation de poly(terephtalate d'ethylene) par esterification directe et polymerisation avec recuperation et recyclage de l'ethyleneglycol vaporise |
Country Status (11)
Country | Link |
---|---|
US (1) | US4110316A (fr) |
JP (1) | JPS53128697A (fr) |
BR (1) | BR7802316A (fr) |
CA (1) | CA1105192A (fr) |
DE (1) | DE2816056A1 (fr) |
ES (1) | ES468790A1 (fr) |
FR (1) | FR2387258A1 (fr) |
GB (1) | GB1585343A (fr) |
IT (1) | IT1158683B (fr) |
MX (1) | MX147181A (fr) |
NL (1) | NL7803999A (fr) |
Families Citing this family (63)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5236558A (en) * | 1982-09-23 | 1993-08-17 | Allied-Signal Inc. | Method to recycle spent ethylene glycol |
DE3544551C2 (de) * | 1985-12-17 | 2002-02-28 | Zimmer Ag | Verfahren zur kontinuierlichen Herstellung von hochmolekularem Polybutylenterephthalat |
US5645936A (en) * | 1986-01-30 | 1997-07-08 | E. I. Du Pont De Nemours And Company | Continuous filaments, yarns, and tows |
EP0501543B1 (fr) * | 1991-02-28 | 1998-05-20 | Agfa-Gevaert N.V. | Méthode pour la production de polyesters à conductivité électrique augmentée |
DE4306144A1 (de) * | 1993-02-27 | 1994-09-01 | Brown John Deutsche Eng Gmbh | Verfahren und Polykondensationsanlage zur Aufbereitung von verunreinigtem Ethylenglykol |
US5296587A (en) * | 1993-03-22 | 1994-03-22 | Eastman Chemical Company | Copolymerization of dicarboxylic acids and dialkyl esters of dicarboxylic acids to form polyesters |
DE19509957A1 (de) * | 1995-03-18 | 1996-09-19 | Basf Ag | Verfahren zur Aufarbeitung von Dihydroxyverbindungen enthaltenden Rückständen |
DE19516886A1 (de) * | 1995-05-09 | 1996-11-14 | Brown John Deutsche Eng Gmbh | Verfahren und Anlage zum Rückgewinnen von Ethylen-Glykol in einem Polyethylenterephthalat-Polykondensationsprozeß |
US5559205A (en) * | 1995-05-18 | 1996-09-24 | E. I. Du Pont De Nemours And Company | Sulfonate-containing polyesters dyeable with basic dyes |
KR100443389B1 (ko) * | 1995-12-14 | 2004-11-16 | 이.아이,듀우판드네모아앤드캄파니 | 폴리에스테르 예비중합체의 제조 방법 |
US6037055A (en) * | 1997-02-12 | 2000-03-14 | E. I. Du Pont De Nemours And Company | Low pill copolyester |
US5817740A (en) * | 1997-02-12 | 1998-10-06 | E. I. Du Pont De Nemours And Company | Low pill polyester |
US6350895B1 (en) | 1999-03-26 | 2002-02-26 | E. I. Du Pont De Nemours And Company | Transesterification process using yttrium and samarium compound catalystis |
US6384180B1 (en) | 1999-08-24 | 2002-05-07 | Eastman Chemical Company | Method for making polyesters employing acidic phosphorus-containing compounds |
US6353062B1 (en) † | 2000-02-11 | 2002-03-05 | E. I. Du Pont De Nemours And Company | Continuous process for producing poly(trimethylene terephthalate) |
EP1259558B2 (fr) | 2000-02-11 | 2010-04-21 | E.I. Du Pont De Nemours And Company | Procede de production en continu de poly(trimethylene terephtalate) |
US6906164B2 (en) | 2000-12-07 | 2005-06-14 | Eastman Chemical Company | Polyester process using a pipe reactor |
EP1453883B1 (fr) | 2000-12-07 | 2012-11-21 | Grupo Petrotemex, S.A. de C.V. | Procede de preparation de polyester a faible cout mettant en oeuvre un reacteur tubulaire |
DE10155419B4 (de) * | 2001-11-12 | 2005-06-16 | Inventa-Fischer Gmbh & Co. Kg | Verfahren zur kontinuierlichen Herstellung von hochmolekularem Polyester sowie Vorrichtung zur Durchführung des Verfahrens |
US6649263B2 (en) | 2001-11-16 | 2003-11-18 | Honeywell International Inc. | Polyester resin and industrial yarn process |
US7135541B2 (en) | 2003-06-06 | 2006-11-14 | Eastman Chemical Company | Polyester process using a pipe reactor |
US7074879B2 (en) * | 2003-06-06 | 2006-07-11 | Eastman Chemical Company | Polyester process using a pipe reactor |
US7129316B2 (en) * | 2004-01-07 | 2006-10-31 | Invista North America S.A R.L. | Process for the manufacture of polyester via hydrogenation treatment of recycled diol |
US7332548B2 (en) * | 2004-03-04 | 2008-02-19 | Eastman Chemical Company | Process for production of a polyester product from alkylene oxide and carboxylic acid |
US20060264664A1 (en) * | 2005-05-19 | 2006-11-23 | Parker Kenny R | Esterification of an exchange solvent enriched composition |
US7834208B2 (en) | 2005-05-19 | 2010-11-16 | Eastman Chemical Company | Process to produce a post catalyst removal composition |
US7919652B2 (en) * | 2005-05-19 | 2011-04-05 | Eastman Chemical Company | Process to produce an enriched composition through the use of a catalyst removal zone and an enrichment zone |
US7741516B2 (en) * | 2005-05-19 | 2010-06-22 | Eastman Chemical Company | Process to enrich a carboxylic acid composition |
US7432395B2 (en) * | 2005-05-19 | 2008-10-07 | Eastman Chemical Company | Enriched carboxylic acid composition |
US7880031B2 (en) * | 2005-05-19 | 2011-02-01 | Eastman Chemical Company | Process to produce an enrichment feed |
US20060264662A1 (en) * | 2005-05-19 | 2006-11-23 | Gibson Philip E | Esterification of an enriched composition |
US7557243B2 (en) | 2005-05-19 | 2009-07-07 | Eastman Chemical Company | Enriched terephthalic acid composition |
US7304178B2 (en) * | 2005-05-19 | 2007-12-04 | Eastman Chemical Company | Enriched isophthalic acid composition |
US7897809B2 (en) * | 2005-05-19 | 2011-03-01 | Eastman Chemical Company | Process to produce an enrichment feed |
US7884231B2 (en) * | 2005-05-19 | 2011-02-08 | Eastman Chemical Company | Process to produce an enriched composition |
US20060264656A1 (en) * | 2005-05-19 | 2006-11-23 | Fujitsu Limited | Enrichment process using compounds useful in a polyester process |
DE102005053858A1 (de) * | 2005-11-11 | 2007-05-16 | Coperion Waeschle Gmbh & Co Kg | Verfahren und Vorrichtung zur Herstellung von Polyester |
US7524921B2 (en) * | 2005-12-21 | 2009-04-28 | E. I. Du Pont De Nemours And Company | Continuous manufacture of poly(trimethylene terephthalate) |
US7531617B2 (en) * | 2005-12-21 | 2009-05-12 | E. I. Du Pont De Nemours And Company | Continuous process for producing poly(trimethylene terephthalate) |
US7888529B2 (en) * | 2006-03-01 | 2011-02-15 | Eastman Chemical Company | Process to produce a post catalyst removal composition |
US7649109B2 (en) | 2006-12-07 | 2010-01-19 | Eastman Chemical Company | Polyester production system employing recirculation of hot alcohol to esterification zone |
US7943094B2 (en) | 2006-12-07 | 2011-05-17 | Grupo Petrotemex, S.A. De C.V. | Polyester production system employing horizontally elongated esterification vessel |
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 |
US7872089B2 (en) | 2007-07-12 | 2011-01-18 | Eastman Chemical Company | Multi-level tubular reactor with internal tray |
US7829653B2 (en) | 2007-07-12 | 2010-11-09 | Eastman Chemical Company | Horizontal trayed reactor |
US7842777B2 (en) | 2007-07-12 | 2010-11-30 | Eastman Chemical Company | Sloped tubular reactor with divided flow |
US7858730B2 (en) | 2007-07-12 | 2010-12-28 | Eastman Chemical Company | Multi-level tubular reactor with dual headers |
US7868129B2 (en) | 2007-07-12 | 2011-01-11 | Eastman Chemical Company | Sloped tubular reactor with spaced sequential trays |
US7872090B2 (en) | 2007-07-12 | 2011-01-18 | Eastman Chemical Company | Reactor system with optimized heating and phase separation |
US7868130B2 (en) | 2007-07-12 | 2011-01-11 | Eastman Chemical Company | Multi-level tubular reactor with vertically spaced segments |
CN101869818B (zh) * | 2010-06-13 | 2012-08-22 | 浙江逸盛石化有限公司 | 降低对苯二甲酸配料罐内压的方法和装置 |
CN103025791B (zh) | 2010-07-23 | 2015-02-25 | 瑞来斯实业公司 | 使用剧烈搅拌容器的连续聚合工艺 |
EP2857434B1 (fr) | 2012-05-30 | 2019-09-25 | Mitsubishi Gas Chemical Company, Inc. | Procédé de production de résine de polyester |
SG11201510196WA (en) | 2013-06-12 | 2016-01-28 | Basf Se | Device for synthesizing a polymer with reduced formation of deposits in the reaction chamber |
US9604202B2 (en) | 2014-05-08 | 2017-03-28 | Eastman Chemical Company | Furan-2,5-dicarboxylic acid purge process |
US9944615B2 (en) | 2014-05-08 | 2018-04-17 | Eastman Chemical Company | Purifying crude furan 2,5-dicarboxylic acid by hydrogenation and a purge zone |
US10010812B2 (en) | 2014-05-08 | 2018-07-03 | Eastman Chemical Company | Furan-2,5-dicarboxylic acid purge process |
US10421736B2 (en) | 2017-07-20 | 2019-09-24 | Eastman Chemical Company | Production of purified dialkyl-furan-2,5-dicarboxylate (DAFD) in a retrofitted DMT plant |
TWI660964B (zh) | 2018-02-14 | 2019-06-01 | 遠東新世紀股份有限公司 | 磷酸酯穩定劑的製備方法 |
US10344011B1 (en) | 2018-05-04 | 2019-07-09 | Eastman Chemical Company | Furan-2,5-dicarboxylic acid purge process |
US10526301B1 (en) | 2018-10-18 | 2020-01-07 | Eastman Chemical Company | Production of purified dialkyl-furan-2,5-dicarboxylate (DAFD) in a retrofitted DMT plant |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2447778A1 (de) * | 1973-10-16 | 1975-04-17 | Leipzig Chemieanlagen | Verfahren zur vermeidung der anlagerung von festen oligomerepartikeln im kuehler waehrend der kuehlung von spruehglykol bei der kontinuierlichen herstellung von polyaethylenterephthalat (polyester) |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2973341A (en) * | 1956-01-25 | 1961-02-28 | Glanzstoff Ag | Continuous process for production of a polyethylene terephthalate condensate |
BR6458663D0 (pt) * | 1963-04-26 | 1973-12-27 | Fiber Industries Inc | Processo aperfeicoado para a preparacao de polimerosde poliesteres lineares pela esterificacao inicial de acido tereftalico ou trans esterificacao de tereftalato de alquila com um glicol |
DE1570568A1 (de) * | 1964-06-01 | 1970-03-12 | Fiber Industries Inc | Verfahren zur Herstellung von Polykondensationsprodukten |
DE2014818B2 (de) * | 1970-03-26 | 1977-07-28 | Zimmer Ag, 6000 Frankfurt | Verfahren zur kontinuierlichen herstellung von polyaethylenterephthalat |
DE2409343B2 (de) * | 1974-02-27 | 1979-06-28 | Akzo Gmbh, 5600 Wuppertal | Verfahren zum Entfernen der dampfförmigen Reaktionsprodukte bei der Herstellung von Polyestern, insbesondere von Polyäthylenterephthalat |
-
1977
- 1977-04-14 US US05/787,605 patent/US4110316A/en not_active Expired - Lifetime
-
1978
- 1978-04-11 JP JP4183678A patent/JPS53128697A/ja active Pending
- 1978-04-12 CA CA300,958A patent/CA1105192A/fr not_active Expired
- 1978-04-13 FR FR7810883A patent/FR2387258A1/fr active Granted
- 1978-04-13 ES ES468790A patent/ES468790A1/es not_active Expired
- 1978-04-13 MX MX173099A patent/MX147181A/es unknown
- 1978-04-13 IT IT22301/78A patent/IT1158683B/it active
- 1978-04-13 BR BR7802316A patent/BR7802316A/pt unknown
- 1978-04-13 DE DE19782816056 patent/DE2816056A1/de not_active Withdrawn
- 1978-04-13 GB GB14608/78A patent/GB1585343A/en not_active Expired
- 1978-04-14 NL NL7803999A patent/NL7803999A/xx not_active Application Discontinuation
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2447778A1 (de) * | 1973-10-16 | 1975-04-17 | Leipzig Chemieanlagen | Verfahren zur vermeidung der anlagerung von festen oligomerepartikeln im kuehler waehrend der kuehlung von spruehglykol bei der kontinuierlichen herstellung von polyaethylenterephthalat (polyester) |
Also Published As
Publication number | Publication date |
---|---|
GB1585343A (en) | 1981-02-25 |
US4110316A (en) | 1978-08-29 |
IT7822301A0 (it) | 1978-04-13 |
NL7803999A (nl) | 1978-10-17 |
FR2387258B1 (fr) | 1985-05-17 |
IT1158683B (it) | 1987-02-25 |
BR7802316A (pt) | 1978-11-28 |
DE2816056A1 (de) | 1978-10-26 |
CA1105192A (fr) | 1981-07-14 |
ES468790A1 (es) | 1979-09-16 |
MX147181A (es) | 1982-10-20 |
JPS53128697A (en) | 1978-11-09 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
ST | Notification of lapse |