GB648706A - Improvements in or relating to the distillation of hydrochloric acid - Google Patents
Improvements in or relating to the distillation of hydrochloric acidInfo
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B7/00—Halogens; Halogen acids
- C01B7/01—Chlorine; Hydrogen chloride
- C01B7/07—Purification ; Separation
- C01B7/0706—Purification ; Separation of hydrogen chloride
- C01B7/0712—Purification ; 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 Anhydrous hydrogen chloride containing 0.3 to 0.2 per cent water is withdrawn at the top of the tower. Accumulated calcium chloride (50 per cent) solution is withdrawn from receiver 4, neutralized with lime or calcium carbonate in receptacle 6, and concentrated by spraying it into hot gas in tower 7, the liquid flow being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.
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)
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 |
-
1947
- 1947-11-26 GB GB31371/47A patent/GB648706A/en not_active Expired
Cited By (8)
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 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB641429A (en) | Improvements in and relating to the distillation of water | |
IT1008172B (en) | IMPROVEMENT IN VAPOR COMPRESSION DISTILLATION PLANTS | |
GB463770A (en) | An improved process for evaporating liquids | |
GB648706A (en) | Improvements in or relating to the distillation of hydrochloric acid | |
JP2018507163A (en) | Process for the preparation of hydrobromic acid | |
US2640761A (en) | Evaporating apparatus | |
DK172421B1 (en) | Process for the synthesis of ferric chloride | |
US2160832A (en) | Water treatment | |
CN106185842A (en) | A kind of titanium white waste acid enrichment facility | |
US137072A (en) | Improvement in the manufacture of boracic acid | |
GB1449762A (en) | Method for causing condensation in drops on a heat-exchanger tube | |
CN216785766U (en) | Titanium tetrachloride waste acid concentration evaporation plant | |
US1945002A (en) | Process of treating gas | |
GB462191A (en) | Improvements in or relating to a process for the production of water enriched with heavy water | |
SU657006A1 (en) | Device for heat treatment of silica brick | |
SU54883A1 (en) | Method of making vatochnoy acid | |
SU61737A1 (en) | Method for continuous production of ethyl bromide | |
US3408168A (en) | Phosphoric acid concentration | |
US507741A (en) | Eduard luhmann | |
SU633801A1 (en) | Method of obtaining hydrogen chloride | |
US1489915A (en) | Sortium fur elektrochemische industrie g | |
US420830A (en) | Process of recovering glycerine from spent soap-lyes | |
GB742574A (en) | Process and means for the manufacture of alumina | |
GB692882A (en) | Improvements in the recovery of adiponitrile and in apparatus therefor | |
US2030811A (en) | Process for making ammonium salts |