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公开(公告)号:SE7804878A
公开(公告)日:1978-10-29
申请号:SE7804878
申请日:1978-04-27
Applicant: HOECHST AG
Inventor: LEGUTKE G , RECHMEIER G , SCHOLZ H , SCHUCHARDT K , HOLLER E , LIESENFELDER G
IPC: B01J27/00 , C07B61/00 , C07C17/00 , C07C17/156 , C07C19/045 , C07C67/00 , C07C17/15 , C07C19/02
CPC classification number: C07C17/156 , Y02P20/582 , C07C19/045
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公开(公告)号:BR7802608A
公开(公告)日:1978-12-19
申请号:BR7802608
申请日:1978-04-26
Applicant: HOECHST AG
Inventor: SCHUCHARDT K , RECHMEIER G , LIESENFELDER G , SCHOLZ H , LEGUTKE G , HOLLER E
IPC: B01J27/00 , C07B61/00 , C07C17/00 , C07C17/156 , C07C19/045 , C07C67/00 , C07C19/02 , C07C17/15
Abstract: 1,2-dichloroethane is made by subjecting ethylene to an oxychlorination reaction with hydrogen chloride and a gas containing molecular oxygen in gas phase, at elevated temperature and in contact with a fluidized bed copper-II-chloride catalyst on a carrier, wherein the reaction gases are cooled under pressure in two condensation stages, condensed 1,2-dichloroethane and water are removed and the bulk of unreacted starting gas and inert gas are recycled. More specifically the reaction gases are delivered to a third condensation stage and cooled therein under pressure down to a temperature within the range 5 DEG to 18 DEG C. and to the extent necessary for the recycle gas to contain 0.5 to 3 volume % of 1,2-dichloroethane. Next, the recycle gas is directly admixed upstream of the reactor, with a quantity of pure oxygen necessary to replace consumed oxygen and re-establish an oxygen content of 12 to 25 volume % therein.
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公开(公告)号:SE442745B
公开(公告)日:1986-01-27
申请号:SE7804878
申请日:1978-04-27
Applicant: HOECHST AG
Inventor: LEGUTKE G , RECHMEIER G , SCHOLZ H , SCHUCHARDT K , HOLLER E , LIESENFELDER G
IPC: B01J27/00 , C07B61/00 , C07C17/00 , C07C17/156 , C07C19/045 , C07C67/00
Abstract: 1,2-dichloroethane is made by subjecting ethylene to an oxychlorination reaction with hydrogen chloride and a gas containing molecular oxygen in gas phase, at elevated temperature and in contact with a fluidized bed copper-II-chloride catalyst on a carrier, wherein the reaction gases are cooled under pressure in two condensation stages, condensed 1,2-dichloroethane and water are removed and the bulk of unreacted starting gas and inert gas are recycled. More specifically the reaction gases are delivered to a third condensation stage and cooled therein under pressure down to a temperature within the range 5 DEG to 18 DEG C. and to the extent necessary for the recycle gas to contain 0.5 to 3 volume % of 1,2-dichloroethane. Next, the recycle gas is directly admixed upstream of the reactor, with a quantity of pure oxygen necessary to replace consumed oxygen and re-establish an oxygen content of 12 to 25 volume % therein.
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公开(公告)号:SE7804878L
公开(公告)日:1978-10-29
申请号:SE7804878
申请日:1978-04-27
Applicant: HOECHST AG
Inventor: LEGUTKE G , RECHMEIER G , SCHOLZ H , SCHUCHARDT K , HOLLER E , LIESENFELDER G
IPC: B01J27/00 , C07B61/00 , C07C17/00 , C07C17/156 , C07C19/045 , C07C67/00 , C07C17/15 , C07C19/02
Abstract: 1,2-dichloroethane is made by subjecting ethylene to an oxychlorination reaction with hydrogen chloride and a gas containing molecular oxygen in gas phase, at elevated temperature and in contact with a fluidized bed copper-II-chloride catalyst on a carrier, wherein the reaction gases are cooled under pressure in two condensation stages, condensed 1,2-dichloroethane and water are removed and the bulk of unreacted starting gas and inert gas are recycled. More specifically the reaction gases are delivered to a third condensation stage and cooled therein under pressure down to a temperature within the range 5 DEG to 18 DEG C. and to the extent necessary for the recycle gas to contain 0.5 to 3 volume % of 1,2-dichloroethane. Next, the recycle gas is directly admixed upstream of the reactor, with a quantity of pure oxygen necessary to replace consumed oxygen and re-establish an oxygen content of 12 to 25 volume % therein.
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