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Process for the separation of hydrogen chloride gas from a gas mixture obtained in the catalytic oxidation of hydrogen chloride gas with a molecular oxygen-containing gas

机译:从用含分子氧的气体催化氧化氯化氢气体中获得的气体混合物中分离氯化氢气体的方法

摘要

PICT:1009575/C1/1 HCl gas may be separated from a gas mixture obtained by the catalytic oxidation of HCl gas with a molecular oxygen-containing gas, which mixture contains water vapour, by (a) cooling the gases in 2, (b) washing with hydrochloric acid in 5, (c) separating at least a portion of the HCl from (b) into HCl gas and hydrochloric acid azeotrope in 16, (d) washing gases in 5 with water to remove more HCl; conditions being such that the quantities of water vapour drawn off in (d) and the HCl gas from (c) are together equal to the combined quantity of water introduced in (d) and that in the original gases; and the HCl azeotrope from (c) with the dil HCl from (d) is used for washing in (b). The cooling is to 40-150 DEG C. and may be effected by quenching with water and/or HCl. The HCl obtained from (b) may be divided into two portions, one being used for quenching in (a), the other being separated into HCl gas and azeotrope. A condensation step, which may be by cooling, removes a major part of the water vapour. The condensation may be effected by passing up a tower in which cooling water is sprayed. The starting material may contain organic impurities. The oxygen containing gas may be air. Level AB is kept constant by a level controller which operates a temperature controller which in turn operates a control valve which adjusts the relative amounts of HCl flowing along lines 24 and 25. Specifications 908,022, 968,827, 991,081, 1,005,974 and 1,009,574 are referred to.
机译:可以通过(a)在2中冷却气体,将HCl气体从HCl气体与含分子氧的气体催化氧化得到的气体混合物中分离出来,该混合物含有水蒸气。 (b)在5中用盐酸洗涤,(c)从(b)中将至少一部分HCl分离成HCl气体,并在16中分离盐酸共沸物,(d)用水在5中洗涤气体以除去更多的HCl;条件是使在(d)中抽取的水蒸气量和从(c)中抽取的HCl气体量等于(d)中引入的水量与原始气体中的合计量; (c)中的HCl共沸物和(d)中的HCl稀溶液用于(b)中的洗涤。冷却至40-150℃,并且可以通过用水和/或HCl淬灭来进行。从(b)获得的HCl可以分为两部分,一部分用于(a)中的淬灭,另一部分分离成HCl气体和共沸物。可以通过冷却的冷凝步骤去除了大部分的水蒸气。冷凝可通过向上流过冷却水的塔进行。起始原料可以包含有机杂质。含氧气体可以是空气。液位控制器通过操作温度控制器的液位控制器使AB液位保持恒定,而液位控制器又控制控制阀,调节沿管线24和25流动的HCl的相对量。参考规格908,022、968,827、991,081、1,005,974和1,009,574。

著录项

  • 公开/公告号GB1009575A

    专利类型

  • 公开/公告日1965-11-10

    原文格式PDF

  • 申请/专利权人 SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ N.V.;

    申请/专利号GB19630047665

  • 发明设计人

    申请日1963-12-03

  • 分类号C01B7/00;C01B7/01;C01B7/04;

  • 国家 GB

  • 入库时间 2022-08-23 15:35:19

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