Process for purifying crude hydrochloric acid

Distillation: processes – separatory – Distilling to separate or remove only water

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203 22, 203 25, 203 42, 203 80, 55 71, 159 201, 159DIG16, 159DIG19, 202174, 423240R, 423488, B01D 126, C01B 707

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active

051748657

ABSTRACT:
Aqueous hydrochloric acid of very high purity can be obtained in a process for purifying crude aqueous 5 to 20 wt. % hydrochloric acid. In the purification, process water or a water/HCl mixture is evaporated from the crude aqueous hydrochloric acid at a pressure of from 0.01 to 1.0 bar and a temperature of from 10.degree. to 100.degree. C. until a crude, azeotropic mixture of water and HCl is obtained. The crude, azeotropic mixture of water and HCl is distilled in a distillation apparatus at a pressure of from 0.1 to 1.5 bar and a temperature of from 50.degree. to 110.degree. C. A purified gaseous, azeotropic mixture of water and HCl is recovered from the head of the distillation apparatus and a liquid mixture is left at the bottom of the distillation apparatus. The liquid mixture which is left at the bottom of the distillation apparatus is distilled at a pressure of from 0.5 to 2.5 bar and a temperature of from 80.degree. to 130.degree. C.

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patent: 1906467 (1933-05-01), Heath
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patent: 3394056 (1968-07-01), Nadler et al.
patent: 3816599 (1974-06-01), Kafes
patent: 4115531 (1978-09-01), Opitz et al.
patent: 4608120 (1986-08-01), Greenfield et al.
patent: 4617180 (1986-10-01), Vogg

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