Beteiligte Stoffe
| Rolle | Name | HCID | Einwaage |
|---|
| Edukt | Hydrochloric Acid | HCID 313 | — |
| Edukt | 1,1-Dichloroethane | HCID 6365 | — |
| Edukt | 1,1-Difluoroethane | HCID 6368 | — |
| Edukt | Hydrofluoric Acid | HCID 14917 | — |
| Katalysator | Chromium oxide | HCID 165971 | — |
| Produkt | 1,1-Dichloroethane | HCID 6365 | — |
| Produkt | 1,1-Difluoroethane | HCID 6368 | — |
| Produkt | Hydrofluoric Acid | HCID 14917 | — |
| Produkt | 1-Chloro-1-fluoroethane | HCID 15373 | — |
Reaktionsschritte
1,1-Dichloroethane and hydrogen fluoride were introduced into an inconel-made reactor filled with a catalyst (mainly comprising trivalent chromium oxide) and reacted at a reaction temperature of 250° C., the resulting reaction gas, mainly comprising 1,1-difluoroethane, hydrogen chloride and unreacted hydrogen fluoride, was introduced into a first distillation tower, hydrogen chloride which is a low boiling fraction was mainly separated from the top, and hydrogen fluoride, 1,1-difluoroethane, 1,1-dichloroethane and 1-chloro-1-fluoroethane were mainly separated from the bottom and introduced into a second distillation tower. In the second distillation tower, crude 1,1-difluoroethane mainly comprising 1,1-difluoroethane was obtained from the top and hydrogen fluoride, 1,1-dichloroethane and 1-chloro-fluoroethane were mainly separated from the bottom and recirculated to the above-described reaction step. The obtained crude 1,1-difluoroethane had the following composition.
Herkunft & Nachweise
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patentnummer | US07696392B2 |
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| Quelldatensatz | uspto-grants-2010_04 |
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| ORD ID | ord-74034e474fee411a9c9ba94262a0b2c1 |
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| Quellennotiz | uspto-grants-2010_04 |
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