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Isophthalic Acid → 1,2-Bis(4-hydroxyphenyl)ethane isophthalate

HRID 866729
Notizen
Druckvorschau

Reaktionsgleichung

Reaktionsgleichung von HRID 866729
[C:1]([OH:12])(=[O:11])[C:2]1[CH:10]=[CH:9][CH:8]=[C:4]([C:5]([OH:7])=[O:6])[CH:3]=1.C(O[C:17]1[CH:22]=[CH:21][CH:20]=[CH:19][C:18]=1[CH2:23][CH2:24][C:25]1[CH:30]=[CH:29]C=[CH:27][C:26]=1OC(=O)C)(=O)C.[C:35](=[O:38])([O-])[O-].[K+].[K+]>>[C:1]([OH:12])(=[O:11])[C:2]1[CH:10]=[CH:9][CH:8]=[C:4]([C:5]([OH:7])=[O:6])[CH:3]=1.[OH:6][C:21]1[CH:20]=[CH:19][C:18]([CH2:23][CH2:24][C:25]2[CH:30]=[CH:29][C:35]([OH:38])=[CH:27][CH:26]=2)=[CH:17][CH:22]=1
KomponentenReaktionsbedingungenVersuchsvorschriftAufarbeitungQuellen und NachweiseNotizen zur Reaktion

Komponenten

4

Edukt 3

HCID 8496Isophthalic AcidHCID 11430Potassium CarbonateHCID 27493801,2-Bis(acetoxyphenyl)ethane2×

Produkt 1

HCID 64548181,2-Bis(4-hydroxyphenyl)ethane isophthalate

Reaktionsbedingungen

Temperatur
245 °C

Versuchsvorschrift

A charge consisting of 167 parts of isophthalic acid and 298 parts of 1,2-bis(acetoxyphenyl)ethane and 0.005 mols potassium carbonate per mol of 1,2-bis(acetoxyphenyl)ethane is placed in a reaction vessel equipped with a stirrer, condenser and receiver. The vessel is evacuated and purged with nitrogen three times. During the reaction a nitrogen blanket is maintained in the reactor. The temperature is raised to about 245° C. and acetic acid distills. The rate of distillation during the initial 67 percent of reaction is 1.82 ml mol-1 min.-1. The distillation rate tapers after 87 parts of acetic acid have distilled in 55 minutes. The temperature rises slowly to 270° C. during the initial stage. Thereupon the vessel is evacuated to a pressure of about 200 torr for about 5 minutes and the pressure is then slowly reduced to about 1 torr while the temperature is increased to about 290° C. When the amperage on the stirrer motor increases by 0.02 to 0.04 amps, the stirrer motor is switched off and the vacuum is released with nitrogen. A total of 112 parts of acetic acid (98 percent of theoretical) is collected. The rate of evolution of acetic acid during the vacuum stage is 1.67 ml mol-1 min.-1. The prepolymer is extruded from the vessel under slight nitrogen pressure and is reduced in a mill to a powder of particle size in the range of from 0.1 to 0.25 mm. The inherent viscosity of the prepolymer is 0.28. The prepolymer is off white in color.

Aufarbeitung

  1. customis placed in a reaction vessel
  2. customequipped with a stirrer, condenser
  3. customThe vessel is evacuated
  4. custompurged with nitrogen three times
  5. customDuring the reaction a nitrogen blanket
  6. temperatureis maintained in the reactor
  7. distillationacetic acid distills
  8. distillationThe rate of distillation during the initial
  9. custom67 percent of reaction
  10. distillationThe distillation rate tapers after 87 parts of acetic acid have distilled in 55 minutes
  11. customrises slowly to 270° C.
  12. customThereupon the vessel is evacuated to a pressure of about 200 torr for about 5 minutes
  13. temperatureis increased to about 290° C
  14. temperatureWhen the amperage on the stirrer motor increases by 0.02 to 0.04 amps
  15. customA total of 112 parts of acetic acid (98 percent of theoretical) is collected

Quellen und Nachweise

ORD-Eintrag
ord-bb587d78da1e479f9e08c4da8d6c4e53
Quelldatensatz
uspto-grants-1978_07
DOI
10.6084/m9.figshare.5104873.v1
Patentnummer
US04101517

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