GB841374A - Purification of saline water by crystallization with a volatile refrigerant - Google Patents

Purification of saline water by crystallization with a volatile refrigerant

Info

Publication number
GB841374A
GB841374A GB27922/57A GB2792257A GB841374A GB 841374 A GB841374 A GB 841374A GB 27922/57 A GB27922/57 A GB 27922/57A GB 2792257 A GB2792257 A GB 2792257A GB 841374 A GB841374 A GB 841374A
Authority
GB
United Kingdom
Prior art keywords
ice
refrigerant
brine
water
vessel
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
Application number
GB27922/57A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ExxonMobil Technology and Engineering Co
Original Assignee
Exxon Research and Engineering Co
Esso Research and Engineering Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Exxon Research and Engineering Co, Esso Research and Engineering Co filed Critical Exxon Research and Engineering Co
Publication of GB841374A publication Critical patent/GB841374A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/22Treatment of water, waste water, or sewage by freezing

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Physical Water Treatments (AREA)

Abstract

841,374. Purifying water by freezing. ESSO RESEARCH & ENGINEERING CO. Sept. 4, 1957 [Sept. 11, 1956], No. 27922/57. Class 29 A method of purifying brine by freezing includes the steps of contacting the brine in a freezing zone with a liquid refrigerant having a higher vapour pressure than water thus vaporizing the refrigerant and forming a slurry of ice crystals in more concentrated brine, removing the vaporized refrigerant from the freezing zone and compressing and cooling it, removing a slurry of ice and concentrated brine from the freezing zone, separating the ice from the brine and washing the ice with water of a lower salt content than the original brine, removing the ice from the water, bringing the ice into contact with the cooled compressed refrigerant to condense the refrigerant and melt the ice, and stripping the melted ice of refrigerant and recirculating the refrigerant to the freezing zone. Brine is pumped through a precooler 3 to a freezing vessel 4, containing a stirrer 5, and liquid refrigerant in droplet form is bubbled through the brine from pipe 8. The resultant ice slurry and some concentrated brine is removed continuously or in batches to a settling vessel 111 from where the ice is passed by line 110 to a filter 11 where the ice is washed and separated from the brine, or by line 114 to a slurry pump 34 from which it is led to a washer 21 where the ice crystals are freed of interstitial brine. Salt free ice water is passed to the upper part of the washer 21 by line 37 to act as the suspension medium for the rising ice crystals. The layers of salt free water and brine are kept distinct by slowly extracting through pipe 32 liquid at the boundary of the two layers. The slurry is led by line 22 to the condensing vessel 16 where it is brought into direct contact with compressed gaseous refrigerant which has been drawn from the freezing vessel 4 by compressor 12 and passed through a cooler 14 The refrigerant in condensing melts the ice crystals and is preferably immiscible with water so that it stratifies at the top of the condensing vessel and is drawn off through line 18. Fresh water is drawn from the bottom of the vessel through line 23 and, to displace the refrigerant, is led to a stripper 24 in a form of a fractionating column into which steam or warm inert gas is fed by line 25. Volatile refrigerant is vaporized and drawn off by pipe 26 and cooled at 27. Water condensate may be refluxed to the stripper 24. Uncondensed vapour and gas is led to a receiver 129 where the refrigerant stratifies on the fresh water and is drawn off through line 131. Fresh water is drawn from the bottom of the stripper. If only the filter 11 is used to separate ice and brine, the washer 21 is omitted and the ice crystals are washed in the filter and then reslurried with water of low salt content taken from the bottom of the condensing vessel before the crystals are passed to the condensing vessel. Two freezing vessels may be used in series in the brine circuit, with separate compressors having the same discharge pressure and with the second vessel maintained at a lower pressure than the first. The refrigerant after extraction from the condensing vessel, stripper and receiver 129 is returned to the freezing zone through expansion -valve 19. Propane is the preferred refrigerant.
GB27922/57A 1956-09-11 1957-09-04 Purification of saline water by crystallization with a volatile refrigerant Expired GB841374A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US841374XA 1956-09-11 1956-09-11

Publications (1)

Publication Number Publication Date
GB841374A true GB841374A (en) 1960-07-13

Family

ID=22183103

Family Applications (1)

Application Number Title Priority Date Filing Date
GB27922/57A Expired GB841374A (en) 1956-09-11 1957-09-04 Purification of saline water by crystallization with a volatile refrigerant

Country Status (1)

Country Link
GB (1) GB841374A (en)

Cited By (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3137555A (en) * 1961-03-23 1964-06-16 North American Aviation Inc Water purification process using an absorption refrigeration cycle
US3167401A (en) * 1960-04-26 1965-01-26 Chem & Phosphates Ltd Incremental heat transfer including direct contact of volatile liquids
US3170778A (en) * 1961-03-23 1965-02-23 Weston Roy F Inc Desalting sea water
US3180102A (en) * 1961-12-29 1965-04-27 Exxon Research Engineering Co Method of fractionally crystallizing solutions with an immiscible liquid coolant
US3183679A (en) * 1961-03-23 1965-05-18 Struthers Scientific Int Corp Removing refrigerant contaminants and dissolved gases in a fractional crystallization process
US3205078A (en) * 1961-08-10 1965-09-07 Cherry Burrell Corp Method of concentrating citrus juice
US3217505A (en) * 1961-08-11 1965-11-16 Lummus Co Process of purifying aqueous solutions with hydrate formers
US3218817A (en) * 1962-04-02 1965-11-23 Phillips Petroleum Co Fractional crystallization
US3232218A (en) * 1961-12-22 1966-02-01 American Mach & Foundry Process of separating anice-brine slurry
US3234747A (en) * 1961-07-03 1966-02-15 Little Inc A Crystal forming and melting by varying applied pressure
US3240025A (en) * 1962-07-05 1966-03-15 Phillips Petroleum Co Concentrating beer containing carbon dioxide by crystallization at elevated pressure
US3240024A (en) * 1961-11-08 1966-03-15 Carrier Corp Freeze crystallization separation systems
US3253419A (en) * 1963-04-29 1966-05-31 Phillips Petroleum Co Batch fractional crystallization and purification
US3266263A (en) * 1962-06-11 1966-08-16 Phillips Petroleum Co Concentration of aqueous solutions by crystallization with sonic defoaming
US3269134A (en) * 1962-05-16 1966-08-30 Desalination Plants Separating a solvent from solution in indirect and direct freeze units
US3285022A (en) * 1963-01-08 1966-11-15 John W Pike Concentration of extracts by freezing
US3285025A (en) * 1963-12-20 1966-11-15 Phillips Petroleum Co Multi-stage crystallization process
US3285024A (en) * 1963-12-16 1966-11-15 Phillips Petroleum Co Crystal melting with heat pump and heated mother liquid
US3305456A (en) * 1963-06-27 1967-02-21 Universal Oil Prod Co Multiple effect evaporation process
US3344616A (en) * 1963-08-23 1967-10-03 Owen Margaret Louise Desalinization
US3411992A (en) * 1967-12-11 1968-11-19 Electronic Associates Distillation utilizing a vapor compressor and an immiscible liquidsolid medium
WO2013060712A1 (en) * 2011-10-24 2013-05-02 Frederick Simon Oosthuizen Method and apparatus for treatment of effluent accumulating in a desalination plant

Cited By (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3167401A (en) * 1960-04-26 1965-01-26 Chem & Phosphates Ltd Incremental heat transfer including direct contact of volatile liquids
US3170778A (en) * 1961-03-23 1965-02-23 Weston Roy F Inc Desalting sea water
US3137555A (en) * 1961-03-23 1964-06-16 North American Aviation Inc Water purification process using an absorption refrigeration cycle
US3183679A (en) * 1961-03-23 1965-05-18 Struthers Scientific Int Corp Removing refrigerant contaminants and dissolved gases in a fractional crystallization process
US3234747A (en) * 1961-07-03 1966-02-15 Little Inc A Crystal forming and melting by varying applied pressure
US3205078A (en) * 1961-08-10 1965-09-07 Cherry Burrell Corp Method of concentrating citrus juice
US3217505A (en) * 1961-08-11 1965-11-16 Lummus Co Process of purifying aqueous solutions with hydrate formers
US3240024A (en) * 1961-11-08 1966-03-15 Carrier Corp Freeze crystallization separation systems
US3232218A (en) * 1961-12-22 1966-02-01 American Mach & Foundry Process of separating anice-brine slurry
US3180102A (en) * 1961-12-29 1965-04-27 Exxon Research Engineering Co Method of fractionally crystallizing solutions with an immiscible liquid coolant
US3218817A (en) * 1962-04-02 1965-11-23 Phillips Petroleum Co Fractional crystallization
US3269134A (en) * 1962-05-16 1966-08-30 Desalination Plants Separating a solvent from solution in indirect and direct freeze units
US3266263A (en) * 1962-06-11 1966-08-16 Phillips Petroleum Co Concentration of aqueous solutions by crystallization with sonic defoaming
US3240025A (en) * 1962-07-05 1966-03-15 Phillips Petroleum Co Concentrating beer containing carbon dioxide by crystallization at elevated pressure
US3285022A (en) * 1963-01-08 1966-11-15 John W Pike Concentration of extracts by freezing
US3253419A (en) * 1963-04-29 1966-05-31 Phillips Petroleum Co Batch fractional crystallization and purification
US3305456A (en) * 1963-06-27 1967-02-21 Universal Oil Prod Co Multiple effect evaporation process
US3344616A (en) * 1963-08-23 1967-10-03 Owen Margaret Louise Desalinization
US3285024A (en) * 1963-12-16 1966-11-15 Phillips Petroleum Co Crystal melting with heat pump and heated mother liquid
US3285025A (en) * 1963-12-20 1966-11-15 Phillips Petroleum Co Multi-stage crystallization process
US3411992A (en) * 1967-12-11 1968-11-19 Electronic Associates Distillation utilizing a vapor compressor and an immiscible liquidsolid medium
WO2013060712A1 (en) * 2011-10-24 2013-05-02 Frederick Simon Oosthuizen Method and apparatus for treatment of effluent accumulating in a desalination plant

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