ES337977A1 - A procedure for the production of linear polymers of low molecular weight of tereftal acid and ethylenglicol. (Machine-translation by Google Translate, not legally binding) - Google Patents
A procedure for the production of linear polymers of low molecular weight of tereftal acid and ethylenglicol. (Machine-translation by Google Translate, not legally binding)Info
- Publication number
- ES337977A1 ES337977A1 ES337977A ES337977A ES337977A1 ES 337977 A1 ES337977 A1 ES 337977A1 ES 337977 A ES337977 A ES 337977A ES 337977 A ES337977 A ES 337977A ES 337977 A1 ES337977 A1 ES 337977A1
- Authority
- ES
- Spain
- Prior art keywords
- translation
- production
- machine
- legally binding
- google translate
- 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
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
A process for the production of polymers, which consists in reacting ethylene glycol and terephthalic acid in molar proportions comprised between 1.0 and less than 2 moles of ethylene glycol per mole of terephthalic acid in the presence of a pre-formed amount of such polymers, at a temperature between 200º and 300ºC and at a pressure lower than the vapor pressure of ethylene glycol at the reaction temperature. (Machine-translation by Google Translate, not legally binding)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US53664466A | 1966-03-23 | 1966-03-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
ES337977A1 true ES337977A1 (en) | 1968-03-16 |
Family
ID=24139330
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES337977A Expired ES337977A1 (en) | 1966-03-23 | 1967-03-13 | A procedure for the production of linear polymers of low molecular weight of tereftal acid and ethylenglicol. (Machine-translation by Google Translate, not legally binding) |
Country Status (6)
Country | Link |
---|---|
AT (1) | AT273501B (en) |
BE (1) | BE696000A (en) |
DE (1) | DE1720634A1 (en) |
ES (1) | ES337977A1 (en) |
LU (1) | LU53265A1 (en) |
NL (1) | NL6704303A (en) |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
PL224046B1 (en) | 2000-12-07 | 2016-11-30 | Eastman Chem Co | Low cost method for producing polyester using the tubular reactor |
US6906164B2 (en) | 2000-12-07 | 2005-06-14 | Eastman Chemical Company | Polyester process using a pipe reactor |
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 |
US7829653B2 (en) | 2007-07-12 | 2010-11-09 | Eastman Chemical Company | Horizontal trayed reactor |
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 |
US7847053B2 (en) | 2007-07-12 | 2010-12-07 | Eastman Chemical Company | Multi-level tubular reactor with oppositely extending segments |
US7868129B2 (en) | 2007-07-12 | 2011-01-11 | Eastman Chemical Company | Sloped tubular reactor with spaced sequential trays |
US7842777B2 (en) | 2007-07-12 | 2010-11-30 | Eastman Chemical Company | Sloped tubular reactor with divided flow |
US7868130B2 (en) | 2007-07-12 | 2011-01-11 | Eastman Chemical Company | Multi-level tubular reactor with vertically spaced segments |
US7858730B2 (en) | 2007-07-12 | 2010-12-28 | Eastman Chemical Company | Multi-level tubular reactor with dual headers |
-
1967
- 1967-03-13 ES ES337977A patent/ES337977A1/en not_active Expired
- 1967-03-16 DE DE19671720634 patent/DE1720634A1/en active Pending
- 1967-03-23 BE BE696000D patent/BE696000A/xx unknown
- 1967-03-23 NL NL6704303A patent/NL6704303A/xx unknown
- 1967-03-23 AT AT284167A patent/AT273501B/en active
- 1967-03-23 LU LU53265D patent/LU53265A1/xx unknown
Also Published As
Publication number | Publication date |
---|---|
DE1720634A1 (en) | 1971-09-02 |
AT273501B (en) | 1969-08-11 |
BE696000A (en) | 1967-09-25 |
LU53265A1 (en) | 1967-09-25 |
NL6704303A (en) | 1967-09-25 |
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