GB605694A - A process for the recovery of potassium salts from solutions - Google Patents
A process for the recovery of potassium salts from solutionsInfo
- Publication number
- GB605694A GB605694A GB2202539A GB2202539A GB605694A GB 605694 A GB605694 A GB 605694A GB 2202539 A GB2202539 A GB 2202539A GB 2202539 A GB2202539 A GB 2202539A GB 605694 A GB605694 A GB 605694A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acid
- per cent
- salt
- potassium
- dipicrylamine
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/41—Preparation of salts of carboxylic acids
- C07C51/412—Preparation of salts of carboxylic acids by conversion of the acids, their salts, esters or anhydrides with the same carboxylic acid part
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D17/00—Rubidium, caesium or francium compounds
- C01D17/003—Compounds of alkali metals
- C01D17/006—Preparation of potassium compounds comprising precipitating potassium ions by an organic reagent or extracting them by a liquid organic phase
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Removal Of Specific Substances (AREA)
Abstract
To obtain potassium salts from dilute solutions such as p sea-water, a soluble salt of dipicrylamine, such as the calcium, sodium, lithium or magnesium salt is added to precipitate the insoluble potassium salt. The latter is separated and treated with an acid, such as nitric, hydrochloric, sulphuric or acetic acid or with carbon dioxide under pressure, to form the corresponding potassium salt and free dipicrylamine, which is then converted, for instance, into the calcium salt by treatment with a solution of lime. The mother - liquor from which the potassium has been precipitated is treated with an acid such as nitric acid to set free the dipicrylamine from remaining dissolved salt. In the treatment of the potassium dipicrylaminate with nitric acid the acid concentration may be below 20 per cent below 30 DEG C. or 40-50 per cent at above 80 DEG C., the intermediate ranges being unsatisfactory. Hydrochloric acid may be used at 36 per cent and sulphuric acid at 79 per cent strength at 20 DEG C., but hydrochloric acid of 10 per cent may be used at higher temperatures. Quantitative examples are given.ALSO:To obtain potassium salts from dilute solutions such as sea water, a soluble salt of dipicrylamine, such as the calcium, p sodium, lithium or magnesium salt, is added to precipitate the insoluble potassium salt. The latter is separated and treated with an acid, such as nitric, hydrochloric, sulphuric or acetic acid or with carbon dioxide under pressure, to form the corresponding potassium salt and free dipicrylamine, which is then converted, for instance, into the calcium salt by treatment with a solution of lime. The mother-liquor from which the potassium has been precipitated is treated with an acid such as nitric acid to set free the dipicrylamine from remaining dissolved salt. This precipitation is preferably effected by adding the acid in portions at intervals of time such as 10 minutes in order to obtain crystals which are readily separated by filtration. In the treatment of the potassium dipicrylaminate with nitric acid, the acid concentration may be below 20 per cent below 30 DEG C. or 40-50 per cent at above 80 DEG C., the intermediate ranges being unsatisfactory. Hydrochloric acid may be used at 36 per cent and sulphuric acid at 79 per cent strength at 20 DEG C., but hydrochloric acid of 10 per cent may be used at higher temperatures. Quantitative examples are given.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2202539A GB605694A (en) | 1939-07-28 | 1939-07-28 | A process for the recovery of potassium salts from solutions |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2202539A GB605694A (en) | 1939-07-28 | 1939-07-28 | A process for the recovery of potassium salts from solutions |
Publications (1)
Publication Number | Publication Date |
---|---|
GB605694A true GB605694A (en) | 1948-07-29 |
Family
ID=10172687
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2202539A Expired GB605694A (en) | 1939-07-28 | 1939-07-28 | A process for the recovery of potassium salts from solutions |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB605694A (en) |
-
1939
- 1939-07-28 GB GB2202539A patent/GB605694A/en not_active Expired
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