Reaktionsgleichung
[CH:1]([Cl:10])([F:9])[C:2]([F:8])([F:7])[C:3]([Cl:6])([F:5])[F:4].[H][H]>>[CH2:1]([F:9])[C:2]([F:8])([F:7])[CH:3]([F:5])[F:4].[CH:1]([Cl:10])([F:9])[C:2]([F:8])([F:7])[C:3]([Cl:6])([F:5])[F:4]Komponenten
4
Versuchsvorschrift
HCFC-225cb was reduced using the reactor and procedures of Example 2 except that the catalyst was prepared from 0.5% Pd/alumina mixed with 50 cc glass helices. The organics flow rate was 4 cc/hr. with a hydrogen flow rate of 90±10 cc/min. The temperature was maintained at 190°±3° C. for 144 hours. HFC-245ca in an 87-92% selectivity and greater than 98% conversion of HCFC-225cb resulted. As the data from Example 4, shown on Table I below indicate, the Pd/alumina catalyst is stable for 144 hours towards the reduction of HCFC-225cb to HFC-245ca.
Aufarbeitung
- temperatureThe temperature was maintained at 190°±3° C. for 144 hours
Quellen und Nachweise
- ORD-Eintrag
- ord-74d297141d5e4b69b91db61bd8e9dde3
- Quelldatensatz
- uspto-grants-1999_01
- Patentnummer
- US05856594
Verknüpfte Notizen
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