Bromine → Perfluorooctyl bromide

HRID 2209862

反応式

HRID 2209862 の反応式
[F:1][C:2]([F:28])([C:6]([F:27])([F:26])[C:7]([F:25])([F:24])[C:8]([F:23])([F:22])[C:9]([F:21])([F:20])[C:10]([F:19])([F:18])[C:11]([F:17])([F:16])[C:12]([F:15])([F:14])[F:13])C(O)=O.[Br:29]Br.FF>C(O)CO.O>[F:1][C:2]([Br:29])([F:28])[C:6]([F:27])([F:26])[C:7]([F:25])([F:24])[C:8]([F:23])([F:22])[C:9]([F:21])([F:20])[C:10]([F:19])([F:18])[C:11]([F:17])([F:16])[C:12]([F:15])([F:14])[F:13]

参加物

5

反応条件

温度
30 °C

実験手順

Perfluorononanoic acid 100 g (0.215 mole), bromine 41 g (0.258 mole) and Freon 113 (500 ml) were mixed in a 2-liter Teflon plastic bottle. This plastic reactor was equipped with a Teflon-coated magnetic stir bar, inlet and outlet tubes made of Teflon-FEP, and a thermocouple coated with Teflon-FEP. The outlet tube was connected to a condensor which was chilled with an ethylene glycol-water mixture. The acid solution was warmed to 30 ° C. through agitation while the reactor was purged of air by flushing it with an inert gas, such as nitrogen, through the inlet tube; The nitrogen flow was terminated and fluorine gas was bubbled into the mixture at 30 cc/min. The fluorine, supplied by Air Products, was used without further purification. The fluorine flow rate was controlled with a Monel needle valve and monitored with a Hastings mass flow transducer. Despite an exothermic reaction occurring immediately, the reaction temperature was kept at 30°-40° C. throughout the reactor by external cooling. The fluorine flow was maintained until the color of the solution turned from deep red to light yellow. Approximately 2.2 fold excess of fluorine (based on the initial amount of acid used) was required to produce this result. After the fluorine gas was terminated, the reactor was again purged with nitrogen and the mixture was carefully poured into water. The organic precipitate was washed with water containing a small amount of sodium thiosulfite, and then dried over magnesium sulfate. Fractional distillation of the precipitate produced 100 grams of perfluorooctyl bromide (97% yield) having a boiling point between 142°-144° C.

後処理

  1. customThis plastic reactor was equipped with a Teflon-coated magnetic stir bar, inlet and outlet tubes
  2. customwas purged of air
  3. customby flushing it with an inert gas
  4. customThe nitrogen flow was terminated
  5. customfluorine gas was bubbled into the mixture at 30 cc/min
  6. customwas used without further purification
  7. customDespite an exothermic reaction
  8. customwas kept at 30°-40° C. throughout the reactor by external cooling
  9. customto produce this result
  10. customAfter the fluorine gas was terminated
  11. customthe reactor was again purged with nitrogen
  12. additionthe mixture was carefully poured into water
  13. washThe organic precipitate was washed with water containing a small amount of sodium thiosulfite
  14. dry with materialdried over magnesium sulfate
  15. distillationFractional distillation of the precipitate

出典と根拠

ORDレコード
ord-67f5368b6c1d432480ab4bf374479016
出典データセット
uspto-grants-1995_10
特許番号
US05455373

関連ノート

読み込み中…