FIELD: organic chemistry.
SUBSTANCE: 1,2-dichloroethane is obtained by liquid phase ethylene chlorination with discharging of reaction heat due to operation medium boiling. In claimed process nitrogen is added to chlorine and ethylene reagents. Ratio of chlorine volume consumption to nitrogen volume consumption is maintained as 1:1. Reaction is carried out at temperature lower than 1,2-dichloroethane boiling point, and discharging of reaction heat is carried out by evaporative cooling of operation medium in nitrogen.
EFFECT: process of increased selectivity; decreased yield of by-products.
1 tbl, 5 dwg
Title | Year | Author | Number |
---|---|---|---|
NOZZLE REACTOR FOR PRODUCTION OF 1.2-DICHLOROETHANE | 2005 |
|
RU2292945C2 |
VACUUM REACTOR FOR LIQUID-PHASE CHLORINATION OF ETHYLENE | 2004 |
|
RU2303483C2 |
VACUUM PROCESS FOR PRODUCTION OF 1,2-DICHLOROETHANE | 2005 |
|
RU2301793C2 |
BUBBLE KETTLE FOR LIQUID-PHASE ETHYLENE CHLORINATION WITH DISPENSED REAGENT SUPPLY | 2006 |
|
RU2328339C2 |
DISH-SHAPED REACTOR FOR PRODUCING 1,2-DICHLOROETHANE | 2006 |
|
RU2328340C2 |
METHOD FOR PREPARING 1,2-DICHLOROETHANE WITH PRELIMINARY HEATING REAGENTS | 2005 |
|
RU2299875C2 |
METHOD FOR PREPARING 1,2-DICHLOROETHANE WITH COMBINED ELIMINATION OF HEAT | 2005 |
|
RU2299876C2 |
REACTOR FOR DIRECT CHLORINATION OF ETHYLENE | 2007 |
|
RU2367511C2 |
METHOD OF SYNTHESIS OF 1,2-DICHLOROETHANE | 2000 |
|
RU2186759C2 |
METHOD OF PREPARING 1,2-DICHLOROETHANE | 2000 |
|
RU2162834C1 |
Authors
Dates
2006-08-27—Published
2005-02-24—Filed