Patent ID: 8097232

Claim:
A process for preparing chlorine from hydrogen chloride, which comprises: a) feeding of a stream a 1 comprising hydrogen chloride and of a stream a 2 comprising oxygen into an oxidation zone to effect catalytic oxidation of hydrogen chloride to chlorine, giving a product gas stream a 3 comprising chlorine, water, oxygen, carbon dioxide and inert gases; b) cooling the product gas stream a 3 to effect removal of water and hydrogen chloride as aqueous hydrochloric acid, leaving a gas stream b comprising chlorine, water, oxygen, carbon dioxide and inert gases; c) drying the gas stream b) to leave a gas stream c which is substantially free of water and comprises chlorine, oxygen, carbon dioxide and inert gases; d) effecting at least partial liquefaction of the gas stream c and of a chlorine-rich recycle stream f 1 comprising chlorine, oxygen and carbon dioxide by compression and cooling, giving an at least partially liquefied stream d; e) separating compressed stream d into gas stream e 1 comprising chlorine, oxygen, carbon dioxide and inert gases and liquid stream e 2 comprising chlorine, oxygen and carbon dioxide, by introducing said compressed stream d into the top of a column and recirculating part of the liquid stream e 2 to the top of the column, with the oxygen dissolved in the liquid stream e 2 and any dissolved inert gases being stripped out of the recirculated descending liquid stream e 2 by a gas stream ascending in the column, and carbon dioxide present in the ascending gas stream being simultaneously dissolved out of the gas stream by the descending liquid stream wherein at least part of the gas stream e 1 and/or a gas stream f 2 which is low in chlorine and comprises chlorine, oxygen and carbon dioxide is recirculated into the oxidation zone; f) feeding of at least part of the gas stream e 1 into a membrane separation unit and fractionating by membrane separation to give the chlorine-rich recycle stream f 1 and a gas stream f 2 which is low in chlorine and comprises chlorine, oxygen and carbon dioxide and recirculating said chlorine-rich recycle stream f 1 to the compression and cooling d); and g) separating liquid stream e 2 by distillation into a chlorine stream g 1 and a stream g 2 consisting essentially of oxygen and carbon dioxide, wherein at least part of the gas stream e 1 and/or f 2 is recirculated to the oxidation zone a).