Recovery of hydrogen chloride from gaseous product streams...

F - Mech Eng,Light,Heat,Weapons – 25 – J

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F25J 3/02 (2006.01) B01D 53/00 (2006.01) C01B 7/01 (2006.01) F25J 3/06 (2006.01) C01B 7/00 (2006.01)

Patent

CA 1044591

ABSTRACT OF THE DISCLOSURE High purity hydrogen chloride is recovered from a gaseous product stream consisting essentially of hydrogen chloride and at least one chlorinated hydrocarbon of from one to two carbon. atoms, such as the chloromethanes, by a process which has significantly lowered refrigeration requirements, thus resulting in savings of energy and materials. The process involves (a) condensing essentially all of the gaseous stream to form a liquid phase feed stream wherein the liquid phase consists essentially of the hydrogen chloride and the chlorinated hydrocar- bon(s); (b) passing the condensed liquid phase feed stream to a stripping zone; (c) maintaining the stripping zone at a pressure and temperature profile sufficient to retain essentially all of the chlorinated hydrocarbon(s) in a liquid phase and to allow essentially all of the hydrogen chloride to separate in a vapor phase; (d) removing a first recovery stream consisting of the high purity hydrogen chloride vapor phase from the stripping zone; and (e) removing a second recovery stream consisting of the chlorinated hydrocarbon(s) liquid phase from the stripping zone. In a preferred embodiment the gaseous product stream is from a methyl chloride thermal chlorinator and consists essentially of hydrogen chloride and a chloromethanes mixture, this gaseous product stream is completely condensed and cooled to a temperature between about -30°C and about -10°C and then fed to the stripping zone which is maintained at a pressure between about 200 psia and about 250 psia. -1-

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