GB1370344A - Production of chlorinated hydrocarbons - Google Patents
Production of chlorinated hydrocarbonsInfo
- Publication number
- GB1370344A GB1370344A GB4460471A GB4460471A GB1370344A GB 1370344 A GB1370344 A GB 1370344A GB 4460471 A GB4460471 A GB 4460471A GB 4460471 A GB4460471 A GB 4460471A GB 1370344 A GB1370344 A GB 1370344A
- Authority
- GB
- United Kingdom
- Prior art keywords
- bed
- seconds
- reactor
- chlorinated hydrocarbons
- sept
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/093—Preparation of halogenated hydrocarbons by replacement by halogens
- C07C17/15—Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination
- C07C17/152—Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination of hydrocarbons
- C07C17/156—Preparation of halogenated hydrocarbons by replacement by halogens with oxygen as auxiliary reagent, e.g. oxychlorination of hydrocarbons of unsaturated hydrocarbons
Abstract
1370344 Chlorinated hydrocarbons FMC CORP 24 Sept 1971 [28 Sept 1970] 44604/71 Heading C2C Trichloroethylene and perchloroethylene are prepared by continuously feeding ethylene, chlorine and oxygen to a reactor containing a fluidized bed of Deacon-type catalyst and having above the free upper surface of the bed a disengaging space, the mol. ratio of oxygen to ethylene being in the range of 1À05 : 1 to 1À2 : 1 and the atomic ratio of Cl : C in the feed being 1À45 : 1 to 1À85 : 1, the temperature of the bed being 415-435‹ C., the residence time in said reactor being at least 40 seonds and in the bed at least 30 seconds (based on the actual fluidized bed volume) or at least 30 seconds in the reactor and at least 20 seconds in the bed (based on the bed volume at minimum fluidization).
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US7629570A | 1970-09-28 | 1970-09-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1370344A true GB1370344A (en) | 1974-10-16 |
Family
ID=22131086
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4460471A Expired GB1370344A (en) | 1970-09-28 | 1971-09-24 | Production of chlorinated hydrocarbons |
Country Status (2)
Country | Link |
---|---|
GB (1) | GB1370344A (en) |
ZA (1) | ZA715778B (en) |
-
1971
- 1971-08-30 ZA ZA715778A patent/ZA715778B/en unknown
- 1971-09-24 GB GB4460471A patent/GB1370344A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
AU3301371A (en) | 1973-03-08 |
ZA715778B (en) | 1972-04-26 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PLNP | Patent lapsed through nonpayment of renewal fees |