Method for producing 1,2-dichloroethane by means of direct chlorination
AssigneeUhde GmbH
InventorsHarald Hafenscher, Reinhold Weis, Michael Benje
Life of this patent
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AssigneeUhde GmbH
InventorsHarald Hafenscher, Reinhold Weis, Michael Benje
Estimating the term…
The invention relates to a method for producing high-purity 1,2-dichloroethane from dissolved chlorine and dissolved ethylene which are brought into contact with each other using a circulating liquid reaction medium which essentially consists of 1,2-dichloroethane and a catalyst and passes through at least one reaction loop. The two limbs of the loop are connected to a gas-phase stripping container which is arranged at the top and from which the reaction product is outwardly transferred either in a gaseous or liquid form or both in a gaseous form and in a liquid form. The addition points for the addition of chlorine and dissolved ethylene are arranged in the limb of the loop in which the liquid rises. The addition point for dissolved chlorine is always arranged downstream of the ethylene addition point. At least one addition point for liquid 1,2-dichloroethane follows each chlorine addition point, and the addition of the liquid 1,2-dichloroethane is carried out under kinetic energy which is high enough to enable a vigorous mixture of 1,2-dichloroethane, dissolved chlorine and ethylene to be carried out. Preferably, the liquid 1,2-dichloroethane is added by means of at least one jet mixer.
A process for the production of 1,2-dichloroethane of high purity from dissolved chlorine and dissolved ethylene that come into contact with each other in the presence of a circulated liquid reaction agent, the agent primarily consisting essentially of 1,2-dichloroethane and a catalyst, using at least one reaction unit arranged vertically and designed as loop, the two leg sections of the loop communicating with a degassing vessel arranged above the unit, the degassing vessel serving for the withdrawal of the reaction product in gaseous or liquid form or in both forms, the feed points for chlorine and dissolved ethylene being located in the loop leg section in which the liquid ascends, any upstream feed point for ethylene being followed by a downstream feed point for dissolved chlorine, wherein
Dependencies are inferred from the claim text.