GB1218413A - Process for the simultaneous preparation of 1,2-dichloroethane, 1,1,2-trichloroethane and 1,1,2,2-tetrachloroethane using a fixed bed - Google Patents
Process for the simultaneous preparation of 1,2-dichloroethane, 1,1,2-trichloroethane and 1,1,2,2-tetrachloroethane using a fixed bedInfo
- Publication number
- GB1218413A GB1218413A GB2367168A GB2367168A GB1218413A GB 1218413 A GB1218413 A GB 1218413A GB 2367168 A GB2367168 A GB 2367168A GB 2367168 A GB2367168 A GB 2367168A GB 1218413 A GB1218413 A GB 1218413A
- Authority
- GB
- United Kingdom
- Prior art keywords
- zone
- tetrachloroethane
- trichloroethane
- dichloroethane
- fixed bed
- 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
1,218,413. Oxychlorination process. PRODUITS CHIMIQUES PECHINEY - SAINTGOBAIN. 17 May, 1968 [19 May, 1967], No. 23671/68. Heading C2C. 1,2 - Dichloroethane, 1,1,2 - trichloroethane and 1,1,2,2 - tetrachloroethane are produced simultaneously by oxychlorination of ethylene, in a continuous process that comprises passing a gaseous mixture containing ethylene, hydrogen chloride and molecular oxygen, the molar ratios HCl/C 2 H 4 and O 2 /C 2 H 4 being from 1À8 to 3À0 and from 0À5 to 1À5 respectively, through adjacent or separated first and second zones comprising one or more tubular or multitubular devices and containing fixed bed catalysts, the diameter of the tubes of the second zone being greater than the diameter of the tubes of the first zone, the temperature of the warmest region in the first zone being from 250‹ to 400‹ C. and the temperature of the warmest region in the second zone being from 5‹ to 50‹ C. higher than that of the warmest region in the first zone but lying within the range 255‹ to 410‹ C. A fraction of the reactants may be supplied directly to the second reactor in the form of a gas comprising one or more of them. Specified catalyst supports are alumina, silica, silicates, clays, aluminosilicates, magnesia and graphite. Vinyl chloride and/or other chlorinated ethylenes may be produced as by products.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR106970 | 1967-05-19 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1218413A true GB1218413A (en) | 1971-01-06 |
Family
ID=8631132
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2367168A Expired GB1218413A (en) | 1967-05-19 | 1968-05-17 | Process for the simultaneous preparation of 1,2-dichloroethane, 1,1,2-trichloroethane and 1,1,2,2-tetrachloroethane using a fixed bed |
Country Status (6)
Country | Link |
---|---|
BE (1) | BE715345A (en) |
CA (1) | CA919712A (en) |
ES (1) | ES354038A1 (en) |
FR (1) | FR1552820A (en) |
GB (1) | GB1218413A (en) |
NL (1) | NL6807061A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1996026171A1 (en) * | 1995-02-22 | 1996-08-29 | Evc Technology Ag | Oxychlorination of ethylene in two stage fixed-bed reactor |
WO1996040431A1 (en) * | 1995-06-07 | 1996-12-19 | The Dow Chemical Company | Catalyst for and method of oxychlorination |
-
1967
- 1967-05-29 FR FR1552820D patent/FR1552820A/fr not_active Expired
-
1968
- 1968-05-17 CA CA020354A patent/CA919712A/en not_active Expired
- 1968-05-17 NL NL6807061A patent/NL6807061A/xx unknown
- 1968-05-17 BE BE715345D patent/BE715345A/xx unknown
- 1968-05-17 GB GB2367168A patent/GB1218413A/en not_active Expired
- 1968-05-18 ES ES354038A patent/ES354038A1/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1996026171A1 (en) * | 1995-02-22 | 1996-08-29 | Evc Technology Ag | Oxychlorination of ethylene in two stage fixed-bed reactor |
CN1067041C (en) * | 1995-02-22 | 2001-06-13 | Evc技术公开股份有限公司 | Oxychlorination of ethylene in two stage fixed-bed reactor |
WO1996040431A1 (en) * | 1995-06-07 | 1996-12-19 | The Dow Chemical Company | Catalyst for and method of oxychlorination |
AU711117B2 (en) * | 1995-06-07 | 1999-10-07 | Dow Chemical Company, The | Method of oxychlorination |
Also Published As
Publication number | Publication date |
---|---|
DE1768493B2 (en) | 1975-11-27 |
CA919712A (en) | 1973-01-23 |
FR1552820A (en) | 1969-01-10 |
ES354038A1 (en) | 1969-10-16 |
DE1768493A1 (en) | 1971-10-21 |
NL6807061A (en) | 1968-11-20 |
BE715345A (en) | 1968-11-18 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PLNP | Patent lapsed through nonpayment of renewal fees |