GB612603A - Evaporating calcium chloride solutions - Google Patents
Evaporating calcium chloride solutionsInfo
- Publication number
- GB612603A GB612603A GB6243/47A GB624347A GB612603A GB 612603 A GB612603 A GB 612603A GB 6243/47 A GB6243/47 A GB 6243/47A GB 624347 A GB624347 A GB 624347A GB 612603 A GB612603 A GB 612603A
- Authority
- GB
- United Kingdom
- Prior art keywords
- calcium chloride
- per cent
- solution
- per
- ton
- 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
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D1/00—Oxides or hydroxides of sodium, potassium or alkali metals in general
- C01D1/04—Hydroxides
- C01D1/42—Concentration; Dehydration
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F11/00—Compounds of calcium, strontium, or barium
- C01F11/20—Halides
- C01F11/24—Chlorides
- C01F11/30—Concentrating; Dehydrating; Preventing the adsorption of moisture or caking
Abstract
Solid hydrated calcium chloride is obtained from aqueous calcium chloride solutions containing between 60 and 75 per cent Ca Cl2 by exposing the solution at a temperature above 120 DEG C. and with a surface area exceeding 10 and preferably 100 square metres per ton to a gas or vapour, in which the partial water vapour pressure is kept below atmospheric pressure and preferably below 400 mm., under adiabatic conditions or under such thermal conditions that not more than 30 ton calories are gained by the system, or not more than 15 ton calories are lost, per ton of product. The ideal process, which is both adiabatic and isothermal, is represented by the use of 72 per cent calcium chloride solution at 170 DEG to 175 DEG C. and is an auto-evaporative-crystallisation process giving solid calcium chloride dihydrate. In an example, a 70 per cent Ca Cl2 solution at 175 DEG C. is sprayed down a vertical empty tower, 15 feet high, in which the pressure is maintained at 5 lbs. per square inch. A granular product containing 76 per cent Ca Cl2, having a bulk density of 0.4 to 0.5 grams per cc. is obtained. In a modification, a 70 per cent Ca Cl2 solution at 170 DEG is sprayed down a tower up which air at 180 DEG C. is blown. Film evaporation may also be used, employing (a) a heat-insulated ribbon mixer in which the solution is evaporated on the surface of granular calcium chloride in a current of air; or (b) a horizontal drum rotating partly in a bath of 72 per cent Ca Cl2 at 175 DEG C. and partly in the atmosphere.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB9116/46A GB612530A (en) | 1946-03-25 | 1946-03-25 | Evaporating caustic soda solutions |
Publications (1)
Publication Number | Publication Date |
---|---|
GB612603A true GB612603A (en) | 1948-11-15 |
Family
ID=26239558
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB9116/46A Expired GB612530A (en) | 1946-03-25 | 1946-03-25 | Evaporating caustic soda solutions |
GB6243/47A Expired GB612603A (en) | 1946-03-25 | 1946-03-25 | Evaporating calcium chloride solutions |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB9116/46A Expired GB612530A (en) | 1946-03-25 | 1946-03-25 | Evaporating caustic soda solutions |
Country Status (7)
Country | Link |
---|---|
US (1) | US2556184A (en) |
BE (2) | BE472116A (en) |
CH (1) | CH275158A (en) |
DE (1) | DE819689C (en) |
FR (1) | FR943963A (en) |
GB (2) | GB612530A (en) |
NL (1) | NL77144C (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3339618A (en) * | 1963-06-13 | 1967-09-05 | Wyandotte Chemicals Corp | Process for preparing powder and granular calcium chloride products |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2635684A (en) * | 1949-05-24 | 1953-04-21 | Ici Ltd | Manufacture of caustic soda granules |
US2882126A (en) * | 1954-11-18 | 1959-04-14 | Columbia Southern Chem Corp | Chemical process |
US2857244A (en) * | 1955-01-03 | 1958-10-21 | Allied Chem | Process for the manufacture of highdensity, anhydrous calcium chloride |
US2839360A (en) * | 1955-02-24 | 1958-06-17 | Michigan Chem Corp | Method for reducing the concentration of alkali metal salts in calcium chloride brines |
US3250593A (en) * | 1964-04-27 | 1966-05-10 | Dow Chemical Co | Method of producing calcium chloride pellets |
JPS5851974A (en) * | 1981-09-21 | 1983-03-26 | Kobe Steel Ltd | Recovery of cacl2 from exhaust gas-desulfurizing waste liquid |
DE3727171A1 (en) * | 1987-08-14 | 1989-02-23 | Krupp Gmbh | Process for the preparation of absolute ethanol |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1026724A (en) * | 1912-05-21 | E N Trump | Porous granular hygroscopic material. | |
US996832A (en) * | 1907-10-02 | 1911-07-04 | Charles H Campbell | Desiccating milk. |
US1166225A (en) * | 1913-07-28 | 1915-12-28 | Georg Alexander Krause | Process of desiccation. |
AT96934B (en) * | 1921-06-04 | 1924-05-10 | Kummler & Matter Ag | Process for evaporating salt solutions. |
US1592971A (en) * | 1925-09-26 | 1926-07-20 | Dow Chemical Co | Prepared metallic chloride and method of making same |
US1660053A (en) * | 1925-10-12 | 1928-02-21 | Dow Chemical Co | Prepared calcium chloride and method of making same |
US1852303A (en) * | 1928-11-06 | 1932-04-05 | Dow Chemical Co | Calcium chloride and method of making same |
US1877733A (en) * | 1930-09-24 | 1932-09-13 | Texas Chemical Products Compan | Anhydrous metallic chlorides and their preparation |
US1907988A (en) * | 1931-06-04 | 1933-05-09 | Pittsburgh Plate Glass Co | Preparation of anhydrous caustic |
US1958034A (en) * | 1933-07-03 | 1934-05-08 | Dow Chemical Co | Processing calcium chloride solution |
US2032727A (en) * | 1934-05-31 | 1936-03-03 | Solvay Process Co | Purification of calcium chloride brines |
US2154672A (en) * | 1935-10-12 | 1939-04-18 | Calorider Corp | Formed bodies of solid calcium chloride hydrate |
-
1946
- 1946-03-25 GB GB9116/46A patent/GB612530A/en not_active Expired
- 1946-03-25 GB GB6243/47A patent/GB612603A/en not_active Expired
-
1947
- 1947-03-21 US US736423A patent/US2556184A/en not_active Expired - Lifetime
- 1947-03-22 NL NL131168A patent/NL77144C/nl active
- 1947-03-25 CH CH275158D patent/CH275158A/en unknown
- 1947-03-25 BE BE472116A patent/BE472116A/en unknown
- 1947-03-25 BE BE472117A patent/BE472117A/en unknown
- 1947-03-26 FR FR943963D patent/FR943963A/en not_active Expired
-
1948
- 1948-10-27 DE DEP309D patent/DE819689C/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3339618A (en) * | 1963-06-13 | 1967-09-05 | Wyandotte Chemicals Corp | Process for preparing powder and granular calcium chloride products |
Also Published As
Publication number | Publication date |
---|---|
GB612530A (en) | 1948-11-15 |
CH275158A (en) | 1951-05-15 |
NL77144C (en) | 1954-09-15 |
BE472116A (en) | 1947-09-15 |
BE472117A (en) | 1947-09-15 |
DE819689C (en) | 1951-11-05 |
FR943963A (en) | 1949-03-23 |
US2556184A (en) | 1951-06-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB612603A (en) | Evaporating calcium chloride solutions | |
SE8803817L (en) | PROCEDURE FOR PREPARATION OF CHLORIDE Dioxide | |
GB864774A (en) | Process for the chlorination of polyethylene | |
GB1005400A (en) | Improvements in or relating to alkali metal sesquicarbonates and carbonates | |
US1748897A (en) | Process for obtaining solid mixtures of alkali-metal hypochlorite and alkali-metal chloride | |
US1583662A (en) | Process of forming sodium compounds | |
GB974164A (en) | Production of epichlorohydrin | |
GB1263867A (en) | Improvements in or relating to the dehydration of aqueous hydrochloric acid | |
GB684016A (en) | Process for the preparation of neutral, inorganic oxide pigments | |
US3485578A (en) | Sodium sesquicarbonate-containing composition and its method of preparation | |
GB635175A (en) | Manufacture of anhydrous caustic potash | |
GB833607A (en) | Production of finely grained masses consisting mainly of calcium silicate or calcium silicate and silicic acid | |
GB813286A (en) | Improvements in the ammonia-soda process | |
GB742386A (en) | Manufacture of ammonium bicarbonate | |
GB771640A (en) | Improvements in or relating to production of isopropyl nitrate | |
GB674808A (en) | Process for the production of chlorine dioxide from chlorates | |
GB1107572A (en) | Process for the manufacture of n-acyl taurides | |
JPS59209629A (en) | White smoke preventing method | |
GB675054A (en) | Improvements in the production of chlorine dioxide-containing gas | |
GB822539A (en) | Process for the preparation of phosphorus pentafluoride | |
GB723715A (en) | Process for the manufacture of fluorochlorethylenes | |
GB943216A (en) | Method of and apparatus for producing chlorine dioxide for immediate use | |
GB778120A (en) | Process of producing reactive magnesium carbonate | |
GB820114A (en) | Process for the manufacture of benzonitrile | |
GB850187A (en) | Production of light highly voluminous silicate or silicon dioxide |