GB192032A - Manufacture of sodium nitrate - Google Patents
Manufacture of sodium nitrateInfo
- Publication number
- GB192032A GB192032A GB20192/22A GB2019222A GB192032A GB 192032 A GB192032 A GB 192032A GB 20192/22 A GB20192/22 A GB 20192/22A GB 2019222 A GB2019222 A GB 2019222A GB 192032 A GB192032 A GB 192032A
- Authority
- GB
- United Kingdom
- Prior art keywords
- nitrate
- sulphate
- crystals
- per cent
- content
- 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
- C01D9/00—Nitrates of sodium, potassium or alkali metals in general
- C01D9/02—Preparation by working-up natural salt mixtures
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Agronomy & Crop Science (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Management, Administration, Business Operations System, And Electronic Commerce (AREA)
Abstract
Crushed caliche together with fines is leached at atmospheric or tepid temperatures, not higher than about 60 DEG C., so as to bring the available nitrate into complete solution. The enriched liquors mixed with stabilizing agents of the kind described in Specification 188,634, to avoid contamination of nitrate with sulphate crystals, are passed through heat exchangers, the temperature range being e.g. 25 DEG C. to 6 DEG C., and then subjected to agitation and further cooling, e.g. to 0 DEG C., in refrigerators to remove a portion of the nitrate content by crystallization. Mother-liquor returns to the leaching tanks through the heat interchangers, and through the ammonia condenser in cases where cooling is effected by ammonia vaporization. Impurities consisting mainly of sodium chloride and sodium sulphate remain in solution at the temperature of the heat interchangers from which nitrate crystals substantially free from sulphate are obtained. Further, with the production of solutions of high concentration in nitrate and in the presence of stabilizing agents, the concentration of sulphate is maintained low enough to permit of the crystallization of substantially pure nitrate during vaporization at or below 0 DEG C. The nitrate product is obtained in crystals of uniform size, has a potassium content of about 0.5 to 0.7 per cent and in general not exceeding 1 per cent, a perchlorate content not in excess of about 0.1 per cent and is relatively non-hygroscopic.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US530437A US1516550A (en) | 1922-01-19 | 1922-01-19 | Manufacture of sodium nitrate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB192032A true GB192032A (en) | 1923-11-26 |
Family
ID=24113638
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB20192/22A Expired GB192032A (en) | 1922-01-19 | 1922-07-24 | Manufacture of sodium nitrate |
Country Status (3)
| Country | Link |
|---|---|
| US (1) | US1516550A (en) |
| FR (1) | FR554535A (en) |
| GB (1) | GB192032A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2545746A (en) * | 1946-10-29 | 1951-03-20 | Borax Cons Ltd | Process for the manufacture of boric acid from sodium borate |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19614645C1 (en) * | 1996-04-13 | 1997-10-30 | Durferrit Thermotechnik Gmbh | Process for the selective recovery of salt components from nitrate-nitrate-hydroxide-containing hardening agent salts |
| CN105036222B (en) * | 2015-08-19 | 2017-06-30 | 石家庄工大化工设备有限公司 | A kind of recovery and treatment method of high-salt wastewater |
| CN109133115A (en) * | 2018-09-14 | 2019-01-04 | 湖北兴发化工集团股份有限公司 | The technique and separation equipment of organic-inorganic phase in a kind of separating and recovering dimethyl sulfoxide abraum salt |
-
1922
- 1922-01-19 US US530437A patent/US1516550A/en not_active Expired - Lifetime
- 1922-07-24 GB GB20192/22A patent/GB192032A/en not_active Expired
- 1922-07-28 FR FR554535D patent/FR554535A/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2545746A (en) * | 1946-10-29 | 1951-03-20 | Borax Cons Ltd | Process for the manufacture of boric acid from sodium borate |
Also Published As
| Publication number | Publication date |
|---|---|
| US1516550A (en) | 1924-11-25 |
| FR554535A (en) | 1923-06-12 |
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