GB820093A - Process for the production of highly concentrated hydrogen chloride and hydrogen bromide - Google Patents

Process for the production of highly concentrated hydrogen chloride and hydrogen bromide

Info

Publication number
GB820093A
GB820093A GB23027/57A GB2302757A GB820093A GB 820093 A GB820093 A GB 820093A GB 23027/57 A GB23027/57 A GB 23027/57A GB 2302757 A GB2302757 A GB 2302757A GB 820093 A GB820093 A GB 820093A
Authority
GB
United Kingdom
Prior art keywords
acid
conduit
steam
hydrogen halide
hydrogen
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB23027/57A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Knapsack AG
Knapsack Griesheim AG
Original Assignee
Knapsack AG
Knapsack Griesheim AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Knapsack AG, Knapsack Griesheim AG filed Critical Knapsack AG
Publication of GB820093A publication Critical patent/GB820093A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B7/00Halogens; Halogen acids
    • C01B7/09Bromine; Hydrogen bromide
    • C01B7/093Hydrogen bromide

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Gas Separation By Absorption (AREA)

Abstract

Highly concentrated hydrogen chloride or hydrogen bromide acid is obtained by treating in an absorption system in two steps a mixture of the hydrogen halide, water in the form of a vapour or steam, and a permanent gas uncondensable under the operating conditions; in the first step the mixture being conducted in countercurrent to hot aqueous hydrohalic acid flowing in from above, this acid being below <PICT:0820093/III/1> the azeotropic composition as regards hydrogen halide content heating the mixture so that the permanent gas leaving at the head of the system absorbs large amounts of steam but small amounts of hydrogen halide, a concentrated hydrohalic acid being removed at the bottom of the system, which acid is processed by boiling to obtain hydrogen halide of 100 per cent strength and an azeotropic acid, and in the second step cooling the gas and vapour mixture leaving at the head of the system in such a manner that nearly the entire portion of hydrogen halide is condensed with only part of the steam. In a typical example 2 cubic metres of a hot permanent gas charged with 162 g. of hydrogen chloride and 150 g. of water vapour are passed through conduit 9 into the absorption tower 1 at a temperature of 20 DEG C. The major part of the water (as steam) and a minor proportion of the hydrochloric acid passes through conduit 3 to a cooler 4 from which the permanent gas escapes through conduit 10 and the dilute acid is removed through conduits 8 and 2 to the absorption tower 1. The stronger acid is removed through conduit 5 to a boiling device 6 and 100 per cent acid is withdrawn through conduit 7 and azeotropic acid leaves by way of conduit 11.
GB23027/57A 1956-07-19 1957-07-19 Process for the production of highly concentrated hydrogen chloride and hydrogen bromide Expired GB820093A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE820093X 1956-07-19

Publications (1)

Publication Number Publication Date
GB820093A true GB820093A (en) 1959-09-16

Family

ID=6736112

Family Applications (1)

Application Number Title Priority Date Filing Date
GB23027/57A Expired GB820093A (en) 1956-07-19 1957-07-19 Process for the production of highly concentrated hydrogen chloride and hydrogen bromide

Country Status (1)

Country Link
GB (1) GB820093A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3523753A (en) * 1966-10-12 1970-08-11 Kalk Chemische Fabrik Gmbh Method of obtaining hydrogen chloride gas,aqueous hydrogen bromide solutions and possibly bromine
CN103318843A (en) * 2013-06-06 2013-09-25 中昊光明化工研究设计院有限公司 Hydrogen bromide gas drying method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3523753A (en) * 1966-10-12 1970-08-11 Kalk Chemische Fabrik Gmbh Method of obtaining hydrogen chloride gas,aqueous hydrogen bromide solutions and possibly bromine
CN103318843A (en) * 2013-06-06 2013-09-25 中昊光明化工研究设计院有限公司 Hydrogen bromide gas drying method

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