GB648706A - Improvements in or relating to the distillation of hydrochloric acid - Google Patents

Improvements in or relating to the distillation of hydrochloric acid

Info

Publication number
GB648706A
GB648706A GB31371/47A GB3137147A GB648706A GB 648706 A GB648706 A GB 648706A GB 31371/47 A GB31371/47 A GB 31371/47A GB 3137147 A GB3137147 A GB 3137147A GB 648706 A GB648706 A GB 648706A
Authority
GB
United Kingdom
Prior art keywords
solution
tower
calcium chloride
anhydrous
per cent
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
GB31371/47A
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.)
Morton Salt Co
Original Assignee
Morton Salt Co
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 Morton Salt Co filed Critical Morton Salt Co
Publication of GB648706A publication Critical patent/GB648706A/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
    • C01B7/01Chlorine; Hydrogen chloride
    • C01B7/07Purification ; Separation
    • C01B7/0706Purification ; Separation of hydrogen chloride
    • C01B7/0712Purification ; Separation of hydrogen chloride by distillation

Abstract

Anhydrous hydrogen chloride is produced by introducing hydrochloric acid into a moving column of lumps of anhydrous calcium chloride at an intermediate position between the ends of the column, withdrawing boiling aqueous calcium chloride solution at approximately 125 DEG C. from one end of the column, introducing the vapours evolved from the boiling solution into said end, and withdrawing anhydrous hydrogen chloride from the opposite end. Dilute hydrochloric acid is supplied through inlet 2 into tower 1 which is constructed of brick, resinous material, or steel lined with tile, and is supplied with lumps of anhydrous calcium chloride by hopper 12. Aqueous calcium chloride solution collects in receiver 4 and is boiled at about 125 DEG C. by communicating boiler 4a; the vapours evolved (steam <PICT:0648706/III/1> plus a minor amount of hydrogen chloride) being introduced into the base of the tower. Anhydrous hydrogen chloride containing 0.3 to 0.2 per cent water is withdrawn at the top of the tower. Accumulated calcium chloride (50 per cent) solution is withdrawn from receiver 4, neutralized with lime or calcium carbonate in receptacle 6, and concentrated by spraying it into hot gas in tower 7, the liquid flow being regulated so as to obtain an approximately 70 per cent solution at the base. Part of the neutralized solution may be completely dehydrated in rotating drum 8 which contains lumps of solid calcium chloride heated to about 400 DEG C. by hot gases from furnace 10. The recovered anhydrous calcium chloride is returned to the top of tower 1. In an alternative method of operation, heater 4a is dispensed with and heat is supplied to the solution in receiver 4 by the direct introduction thereto of the hot 70 per cent solution from the base of tower 7.
GB31371/47A 1940-12-10 1947-11-26 Improvements in or relating to the distillation of hydrochloric acid Expired GB648706A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US648706XA 1940-12-10 1940-12-10

Publications (1)

Publication Number Publication Date
GB648706A true GB648706A (en) 1951-01-10

Family

ID=22058755

Family Applications (1)

Application Number Title Priority Date Filing Date
GB31371/47A Expired GB648706A (en) 1940-12-10 1947-11-26 Improvements in or relating to the distillation of hydrochloric acid

Country Status (1)

Country Link
GB (1) GB648706A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4832935A (en) * 1987-11-04 1989-05-23 Gte Laboratories Incorporated Method for dehydrating hydrogen fluoride
FR2836139A1 (en) * 2002-02-18 2003-08-22 Atofina Drying hydrogen chloride derived from aqueous hydrochloric acid solutions comprises contacting the hydrogen chloride with anhydrous calcium chloride
JP2016500633A (en) * 2012-10-19 2016-01-14 エスジーエル・カーボン・エスイー Method for concentrating an aqueous hydrogen halide solution
CN107720696A (en) * 2017-10-18 2018-02-23 荆门市格林美新材料有限公司 A kind of HCl recovery processing unit in waste liquid
CN108525337A (en) * 2018-05-29 2018-09-14 杭州东日节能技术有限公司 A kind of dilute hydrochloric acid is concentrated in vacuo tower and its application method

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4832935A (en) * 1987-11-04 1989-05-23 Gte Laboratories Incorporated Method for dehydrating hydrogen fluoride
FR2836139A1 (en) * 2002-02-18 2003-08-22 Atofina Drying hydrogen chloride derived from aqueous hydrochloric acid solutions comprises contacting the hydrogen chloride with anhydrous calcium chloride
WO2003070630A1 (en) * 2002-02-18 2003-08-28 Atofina Method for drying hydrogen chloride from hydrochloric aqueous solutions
JP2016500633A (en) * 2012-10-19 2016-01-14 エスジーエル・カーボン・エスイー Method for concentrating an aqueous hydrogen halide solution
CN107720696A (en) * 2017-10-18 2018-02-23 荆门市格林美新材料有限公司 A kind of HCl recovery processing unit in waste liquid
CN107720696B (en) * 2017-10-18 2019-10-11 荆门市格林美新材料有限公司 A kind of HCl recovery processing unit in waste liquid
CN108525337A (en) * 2018-05-29 2018-09-14 杭州东日节能技术有限公司 A kind of dilute hydrochloric acid is concentrated in vacuo tower and its application method
CN108525337B (en) * 2018-05-29 2023-07-18 杭州东日节能技术有限公司 Dilute hydrochloric acid vacuum concentration tower and its use method

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