GB979963A - Improved method and apparatus for water purification by crystallization - Google Patents
Improved method and apparatus for water purification by crystallizationInfo
- Publication number
- GB979963A GB979963A GB30320/61A GB3032061A GB979963A GB 979963 A GB979963 A GB 979963A GB 30320/61 A GB30320/61 A GB 30320/61A GB 3032061 A GB3032061 A GB 3032061A GB 979963 A GB979963 A GB 979963A
- Authority
- GB
- United Kingdom
- Prior art keywords
- crystals
- line
- mother liquor
- saline
- crystallizer
- 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
-
- 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
- B01D9/0009—Crystallisation cooling by heat exchange by direct heat exchange with added cooling fluid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0059—General arrangements of crystallisation plant, e.g. flow sheets
Abstract
979,963. Production of fresh water from saline water by freezing. J. W. PIKE. Aug. 22, 1961, No. 30320/61. Heading F4H. In the production of potable water from a saline solution such as sea water, a super cooled saline solution at a temperature within the metastable condition is mixed with a saline mother liquor having ice crystals suspended therein. Fresh water from the solution in the metastable condition deposits on and expands the size of the ice crystals which can be removed for washing and melting. Saline feed water enters through a line 1 and is cooled in a heat exchanger 4 to substantially the freezing point temperature. It is then mixed with a circulating mother liquor comprising dissolved solids, ice and water in a line 5 and pumped to a higher pressure in order to discharge into an evaporator 7. A volatile liquid hydrocarbon refrigerant such as isobutane is introduced into the mixture in line 5 through a line 14, reducing the temperature of the mixture into the metastable condition, that is 0.05‹ to 1.5‹ F. below the initial freezing point of the mixture. The refrigerant vapour leaves the evaporator by a line 11 and flows to a compressor 12 and a condenser 29 for redelivery through the line 14. The super cooled saline mixture or solution flows through a line 8 into a crystallizer 9 through a centre pipe 10, entering near the top of the crystallizer. The mother liquor in the crystallizer contains a suspension of seed crystals. The fresh water content of the super cooled saline mixture tends to solidify on the crystals present, building these into larger crystals which tend to rise, whilst new crystals are also formed. The super cooled saline mixture on flowing down the crystallizer reacts against the upwardly flowing ice crystals. By maintaining a downward flow in this manner, the crystals may be maintained in suspension whilst they are growing. Finally, large crystals rise to the top of the crystallizer and seed crystals are forced to the bottom to be recirculated with the mother liquor for a repetition of the cooling cycle. Large crystals and mother liquor are continuously removed from the top of the crystallizer by a pump 16 through a line 15 and discharged into a refrigerantremoving vacuum chamber 17. The slurry underflow discharges through a line 21 into a gravity separator 22 where the ice crystals are decanted off through a line 24 to a filter 25. The filtered ice crystals are washed with fresh water delivered through a pipe 30 and are then melted in the refrigerant condenser 29. Residual mother liquor from the filter 25 and mother liquor from the separator 22 pass through the cooling side of the heat exchanger 4. Saline solution is defined as encompassing solutions described as brackish and also sea water. Such solutions may contain salts such as sodium chloride, calcium chloride, magnesium chloride and similar salts formed from alkali earth metals and the halogens. Suitable refrigerators mentioned include certain paraffins and olefinic hydrocarbons which have the required vapour pressure characteristics Among these are butane, propane, propylene, ethylene and ethane.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB30320/61A GB979963A (en) | 1961-08-22 | 1961-08-22 | Improved method and apparatus for water purification by crystallization |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB30320/61A GB979963A (en) | 1961-08-22 | 1961-08-22 | Improved method and apparatus for water purification by crystallization |
Publications (1)
Publication Number | Publication Date |
---|---|
GB979963A true GB979963A (en) | 1965-01-06 |
Family
ID=10305777
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB30320/61A Expired GB979963A (en) | 1961-08-22 | 1961-08-22 | Improved method and apparatus for water purification by crystallization |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB979963A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010060718A1 (en) * | 2008-11-03 | 2010-06-03 | Akzo Nobel N.V. | Sodium chloride production process |
US8771380B2 (en) | 2008-07-22 | 2014-07-08 | Akzo Nobel N.V. | Sodium chloride production process |
CN109745727A (en) * | 2017-11-08 | 2019-05-14 | 中国科学院广州能源研究所 | A kind of crystallization processes Process Energy stepped utilization method and the device for realizing this method |
-
1961
- 1961-08-22 GB GB30320/61A patent/GB979963A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8771380B2 (en) | 2008-07-22 | 2014-07-08 | Akzo Nobel N.V. | Sodium chloride production process |
WO2010060718A1 (en) * | 2008-11-03 | 2010-06-03 | Akzo Nobel N.V. | Sodium chloride production process |
RU2504516C2 (en) * | 2008-11-03 | 2014-01-20 | Акцо Нобель Н.В. | Method of producing sodium chloride |
US8888867B2 (en) | 2008-11-03 | 2014-11-18 | Akzo Nobel N.V. | Sodium chloride production process |
CN109745727A (en) * | 2017-11-08 | 2019-05-14 | 中国科学院广州能源研究所 | A kind of crystallization processes Process Energy stepped utilization method and the device for realizing this method |
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