GB1001787A - A process for the preparation of polyethylene terephthalate - Google Patents
A process for the preparation of polyethylene terephthalateInfo
- Publication number
- GB1001787A GB1001787A GB37273/63A GB3727363A GB1001787A GB 1001787 A GB1001787 A GB 1001787A GB 37273/63 A GB37273/63 A GB 37273/63A GB 3727363 A GB3727363 A GB 3727363A GB 1001787 A GB1001787 A GB 1001787A
- Authority
- GB
- United Kingdom
- Prior art keywords
- ethylene glycol
- terephthalic acid
- reaction medium
- polyethylene terephthalate
- replaced
- 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.)
- Expired
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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL282561 | 1962-09-24 | ||
NL283561 | 1962-09-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1001787A true GB1001787A (en) | 1965-08-18 |
Family
ID=26641845
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB37273/63A Expired GB1001787A (en) | 1962-09-24 | 1963-09-23 | A process for the preparation of polyethylene terephthalate |
Country Status (2)
Country | Link |
---|---|
GB (1) | GB1001787A (enrdf_load_stackoverflow) |
LU (1) | LU44479A1 (enrdf_load_stackoverflow) |
Cited By (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3442868A (en) * | 1965-07-20 | 1969-05-06 | Teijin Ltd | Novel process for the preparation of polyester |
US3487049A (en) * | 1967-01-04 | 1969-12-30 | Du Pont | Process for producing polyethylene terephthalate |
US3496146A (en) * | 1967-08-23 | 1970-02-17 | Du Pont | Preparation of glycol terephthalate linear polyester by direct esterification of terephthalic acid |
JPS4826290A (enrdf_load_stackoverflow) * | 1971-08-11 | 1973-04-06 | ||
JPS4980033A (enrdf_load_stackoverflow) * | 1972-11-10 | 1974-08-02 | ||
US4079046A (en) * | 1976-06-03 | 1978-03-14 | Monsanto Company, St. Louis, Missouri | Multiple polyesterification process |
US7332548B2 (en) | 2004-03-04 | 2008-02-19 | Eastman Chemical Company | Process for production of a polyester product from alkylene oxide and carboxylic acid |
US7345139B2 (en) | 2000-12-07 | 2008-03-18 | Eastman Chemical Company | Polyester process using a pipe reactor |
US7649109B2 (en) | 2006-12-07 | 2010-01-19 | Eastman Chemical Company | Polyester production system employing recirculation of hot alcohol to esterification zone |
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 |
US7847053B2 (en) | 2007-07-12 | 2010-12-07 | Eastman Chemical Company | Multi-level tubular reactor with oppositely extending segments |
US7858730B2 (en) | 2007-07-12 | 2010-12-28 | Eastman Chemical Company | Multi-level tubular reactor with dual headers |
US7863477B2 (en) | 2007-03-08 | 2011-01-04 | Eastman Chemical Company | Polyester production system employing hot paste to esterification zone |
US7868130B2 (en) | 2007-07-12 | 2011-01-11 | Eastman Chemical Company | Multi-level tubular reactor with vertically spaced segments |
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 |
US7872089B2 (en) | 2007-07-12 | 2011-01-18 | Eastman Chemical Company | Multi-level tubular reactor with internal tray |
US7943094B2 (en) | 2006-12-07 | 2011-05-17 | Grupo Petrotemex, S.A. De C.V. | Polyester production system employing horizontally elongated esterification vessel |
-
1963
- 1963-09-21 LU LU44479A patent/LU44479A1/xx unknown
- 1963-09-23 GB GB37273/63A patent/GB1001787A/en not_active Expired
Cited By (29)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3442868A (en) * | 1965-07-20 | 1969-05-06 | Teijin Ltd | Novel process for the preparation of polyester |
US3487049A (en) * | 1967-01-04 | 1969-12-30 | Du Pont | Process for producing polyethylene terephthalate |
US3496146A (en) * | 1967-08-23 | 1970-02-17 | Du Pont | Preparation of glycol terephthalate linear polyester by direct esterification of terephthalic acid |
JPS4826290A (enrdf_load_stackoverflow) * | 1971-08-11 | 1973-04-06 | ||
JPS4980033A (enrdf_load_stackoverflow) * | 1972-11-10 | 1974-08-02 | ||
US4079046A (en) * | 1976-06-03 | 1978-03-14 | Monsanto Company, St. Louis, Missouri | Multiple polyesterification process |
US7420026B2 (en) | 2000-12-07 | 2008-09-02 | Eastman Chemical Company | Polyester process using a pipe reactor |
US7345139B2 (en) | 2000-12-07 | 2008-03-18 | Eastman Chemical Company | Polyester process using a pipe reactor |
US7842778B2 (en) | 2000-12-07 | 2010-11-30 | Eastman Chemical Company | Polyester process using a pipe reactor |
US7423109B2 (en) | 2000-12-07 | 2008-09-09 | Eastman Chemical Company | Polyester process using a pipe reactor |
US7446162B2 (en) | 2000-12-07 | 2008-11-04 | Eastman Chemical Company | Polyester process using a pipe reactor |
US7495067B2 (en) | 2000-12-07 | 2009-02-24 | Eastman Chemical Company | Polyester process using a pipe reactor |
US7531618B2 (en) | 2000-12-07 | 2009-05-12 | Eastman Chemical Company | Polyester process using a pipe reactor |
US7541423B2 (en) | 2000-12-07 | 2009-06-02 | Eastman Chemical Company | Polyester process using a pipe reactor |
US7718759B2 (en) | 2000-12-07 | 2010-05-18 | Eastman Chemical Company | Polyester process using a pipe reactor |
US8114954B2 (en) | 2000-12-07 | 2012-02-14 | Grupo Petrotemex, S.A. De C.V. | Polyester process using a pipe reactor |
US7332548B2 (en) | 2004-03-04 | 2008-02-19 | Eastman Chemical Company | Process for production of a polyester product from alkylene oxide and carboxylic acid |
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 |
US8470250B2 (en) | 2006-12-07 | 2013-06-25 | 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 |
US7842777B2 (en) | 2007-07-12 | 2010-11-30 | Eastman Chemical Company | Sloped tubular reactor with divided flow |
US7847053B2 (en) | 2007-07-12 | 2010-12-07 | Eastman Chemical Company | Multi-level tubular reactor with oppositely extending segments |
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 |
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 |
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 |
Also Published As
Publication number | Publication date |
---|---|
LU44479A1 (enrdf_load_stackoverflow) | 1963-11-21 |
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