GB1240668A - Improvements relating to crystallizing apparatus - Google Patents
Improvements relating to crystallizing apparatusInfo
- Publication number
- GB1240668A GB1240668A GB4873/71A GB487371A GB1240668A GB 1240668 A GB1240668 A GB 1240668A GB 4873/71 A GB4873/71 A GB 4873/71A GB 487371 A GB487371 A GB 487371A GB 1240668 A GB1240668 A GB 1240668A
- Authority
- GB
- United Kingdom
- Prior art keywords
- solution
- chamber
- chambers
- heat exchange
- series
- 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
- 239000000243 solution Substances 0.000 abstract 11
- 239000013078 crystal Substances 0.000 abstract 3
- 238000005192 partition Methods 0.000 abstract 3
- 238000001816 cooling Methods 0.000 abstract 2
- 239000012267 brine Substances 0.000 abstract 1
- 239000012809 cooling fluid Substances 0.000 abstract 1
- 238000002425 crystallisation Methods 0.000 abstract 1
- 239000002002 slurry Substances 0.000 abstract 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 abstract 1
- 239000007921 spray Substances 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D3/00—Halides of sodium, potassium or alkali metals in general
- C01D3/04—Chlorides
- C01D3/06—Preparation by working up brines; seawater or spent lyes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0004—Crystallisation cooling by heat exchange
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0036—Crystallisation on to a bed of product crystals; Seeding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/004—Fractional crystallisation; Fractionating or rectifying columns
Landscapes
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
1,240,668. Multi-stage crystallisation. GARRETT RESEARCH & DEVELOPMENT CO. Inc. 27 June, 1968 [2 May, 1968], No. 4873/ 71. Divided out of 1,240,667. Heading B1G. A multi-stage crystalliser comprises a housing divided by vertical partitions into a series of chambers, each partition having two apertures, an upper and a lower, for interconnecting the chambers, these being such that the crystallizing solution (e.g. a brine) can pass through the series of chambers from a first chamber to a final chamber, the lower aperture being for passage of the crystals through the chambers, they settling to the bottom of each chamber, and the upper connections for passage of the solution through the chambers. Each chamber has a heat exchange means associated therewith for cooling the solution and individual pump means for circulating the solution around the heat exchange means. In the embodiment shown each pump 118 pumps the solution around a circuit from the chamber 112 to sprays 120, the heat exchange medium being upwardly flowing atmospheric air circulated by a fan 124, the cooling tower walls being preferably air permeable. Baffles 108 and the heat exchange mechanism and funnel 110 serves to feed the crystals and solution back to the main body of the solution. The upper inter-chamber connections are at the surface level of the crystallizing solution and the lower 114 are at the bottom of the chamber partitions 104. The crystal slurry outlet is pipe 126, the solution inlet being either or both of pipes 118 and 82. A further embodiment (Fig. 3) has the solution pumped around a circuit including heat exchangers (74) in which pipes carry a common flow of cooling fluid in countercurrent to the direction of flow of the crystallizing solution. For certain purposes both embodiments may be in series, the atmospheric heat exchange type following the other.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US72614968A | 1968-05-02 | 1968-05-02 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1240668A true GB1240668A (en) | 1971-07-28 |
Family
ID=24917444
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB30734/68A Expired GB1240667A (en) | 1968-05-02 | 1968-06-27 | Method of recovering potassium chloride from a brine or like solution |
| GB4873/71A Expired GB1240668A (en) | 1968-05-02 | 1968-06-27 | Improvements relating to crystallizing apparatus |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB30734/68A Expired GB1240667A (en) | 1968-05-02 | 1968-06-27 | Method of recovering potassium chloride from a brine or like solution |
Country Status (1)
| Country | Link |
|---|---|
| GB (2) | GB1240667A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104208899A (en) * | 2013-06-05 | 2014-12-17 | 甘肃瑞川化工有限公司 | Spray air-cooled cooling system |
| CN110694287A (en) * | 2019-09-26 | 2020-01-17 | 浙江环森环境科技有限公司 | Low temperature evaporative crystallizer |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH652110A5 (en) * | 1982-12-23 | 1985-10-31 | Escher Wyss Ag | TREATMENT OF BRINE SLEEPING WITH HIGH NA (2) SO (4) AND KC1 PROPORTION. |
| RU2316604C1 (en) * | 2006-04-03 | 2008-02-10 | Открытое Акционерное Общество "Корпорация Всмпо-Ависма" | Method for processing salt rejects of magnesium production |
| JP2010520143A (en) * | 2007-03-06 | 2010-06-10 | ポタシオ リオ コロラド エス.エー. | How to handle potash |
| RU2341570C1 (en) * | 2007-05-17 | 2008-12-20 | Открытое Акционерное Общество "Корпорация Всмпо-Ависма" | Reprocessing method of saline wastes, containing chlorides of alkaline and/or alkaline-earth metals |
| US8771380B2 (en) * | 2008-07-22 | 2014-07-08 | Akzo Nobel N.V. | Sodium chloride production process |
| CN102203012B (en) | 2008-11-03 | 2014-12-10 | 阿克佐诺贝尔股份有限公司 | Sodium chloride production process |
| FR2951383B1 (en) * | 2009-10-20 | 2012-09-21 | Solvay | PROCESS FOR THE JOINT VALORIZATION OF SOLUBLE SALTS CONTAINED IN A RESIDUE OF AN INDUSTRIAL PROCESS |
| CN107837558A (en) * | 2016-09-21 | 2018-03-27 | 山东豪迈化工技术有限公司 | Crystallizer and method for crystallising |
| RU2669622C1 (en) * | 2018-01-31 | 2018-10-12 | Генкин Михаил Владимирович | Method and reactor for extracting sodium chloride and potassium chloride from polymineral sources |
| CN111803996B (en) * | 2020-08-03 | 2024-08-20 | 河南神马尼龙化工有限责任公司 | Single-chamber vacuum cooling crystallization system |
| AU2021105321B4 (en) * | 2020-11-11 | 2022-10-20 | Brinetec Limited | System and method of treating brines |
-
1968
- 1968-06-27 GB GB30734/68A patent/GB1240667A/en not_active Expired
- 1968-06-27 GB GB4873/71A patent/GB1240668A/en not_active Expired
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104208899A (en) * | 2013-06-05 | 2014-12-17 | 甘肃瑞川化工有限公司 | Spray air-cooled cooling system |
| CN104208899B (en) * | 2013-06-05 | 2016-05-04 | 甘肃瑞川化工有限公司 | Spray air-cooled cooling system |
| CN110694287A (en) * | 2019-09-26 | 2020-01-17 | 浙江环森环境科技有限公司 | Low temperature evaporative crystallizer |
Also Published As
| Publication number | Publication date |
|---|---|
| GB1240667A (en) | 1971-07-28 |
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