GB1013767A - Method and apparatus for purifying liquids - Google Patents

Method and apparatus for purifying liquids

Info

Publication number
GB1013767A
GB1013767A GB1337663A GB1337663A GB1013767A GB 1013767 A GB1013767 A GB 1013767A GB 1337663 A GB1337663 A GB 1337663A GB 1337663 A GB1337663 A GB 1337663A GB 1013767 A GB1013767 A GB 1013767A
Authority
GB
United Kingdom
Prior art keywords
water
chamber
air
coil
refrigerant
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
GB1337663A
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.)
Aqua Chem Inc
Original Assignee
Aqua Chem Inc
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 Aqua Chem Inc filed Critical Aqua Chem Inc
Publication of GB1013767A publication Critical patent/GB1013767A/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
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/10Treatment of water, waste water, or sewage by heating by distillation or evaporation by direct contact with a particulate solid or with a fluid, as a heat transfer medium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/02Evaporators with heating coils
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/16Evaporating by spraying
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/007Energy recuperation; Heat pumps
    • 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
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/045Treatment of water, waste water, or sewage by heating by distillation or evaporation for obtaining ultra-pure water

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

1,013,767. Distilling water. AQUA-CHEM Inc. April 4, 1963 [April 18, 1962; Nov. 16, 1962], No. 13376/63. Heading B1B. [Also in Division F4] Pure water is produced from brackish water by spraying it through rotary atomizer 32 into a stream of air flowing up through chamber 17 which is maintained warm by coil 18; some of the water vaporizes into the air, and the moisture-laden air, after passing through demister 28, is blown by fan 29 down into annular chamber 19 where it is cooled by coil 20 so that the water-vapour condenses yielding pure water, which is withdrawn through outlet 26. The air, reaching the bottom of chamber 19, is recirculated to chamber 17. The cylindrical wall 16, between the two chambers, is made of insulating-material. Coils 18 and 20 form part of a circuit which contains a refrigerant, and includes a compressor 41. Coil 20 is maintained at about 100 ‹F. by the vaporization of the liquid refrigerant and the vapours, after being compressed in compressor 41, flow into coil 18 where they condense at about 140 ‹F. The liquid refrigerant then flows back to coil 20 via restriction 42. Brackish water-to-betreated is introduced into well 14 via inlet 27; and some of the water is drawn up from the well into the hollow shaft 31, which drives fan 29 and atomizer 32. The water flows out of the ports 35 in shaft 31, and is atomized by blades 36. Excess water is drained out of well 14 via outlet 44. An apparatus is also described in which the product water is "Pasteurized", i.e. raised to a temperature of 140-212 ‹F., by heat-exchange with hot refrigerant. The feed water is preheated by heat-exchange with (i) the "Pasteurized" product water, and (ii) the air stream in chamber 19; and the rate of flow of the feed-water is automatically controlled by a valve to maintain the temperature of chamber 17 substantially constant. On-off electrical switches are incorporated in the apparatus so that the compressor and the fan are switched on or off in response to the level or temperature of the pure water in the storage tank. The refrigerant cycle may be replaced by an electric circuit having hot junctions disposed in the heating chamber and cold junctions disposed in the cooling chamber. It is also stated that the heating and cooling may be effected by a compression-expansion cycle of the circulating air. An apparatus is described in which the heating coil is supplied with hot gases from a burner, and the circulating air is blown towards the heating coil by a rotary impeller. The moisture-laden air is cooled in heat-exchange with streams of air at ambient temperature.
GB1337663A 1962-04-18 1963-04-04 Method and apparatus for purifying liquids Expired GB1013767A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US18849662A 1962-04-18 1962-04-18
US23939662A 1962-11-16 1962-11-16

Publications (1)

Publication Number Publication Date
GB1013767A true GB1013767A (en) 1965-12-22

Family

ID=26884132

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1337663A Expired GB1013767A (en) 1962-04-18 1963-04-04 Method and apparatus for purifying liquids

Country Status (4)

Country Link
CH (1) CH447056A (en)
DE (1) DE1517363A1 (en)
GB (1) GB1013767A (en)
NL (2) NL6802024A (en)

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9969638B2 (en) 2013-08-05 2018-05-15 Gradiant Corporation Water treatment systems and associated methods
US10167218B2 (en) 2015-02-11 2019-01-01 Gradiant Corporation Production of ultra-high-density brines
US10245555B2 (en) 2015-08-14 2019-04-02 Gradiant Corporation Production of multivalent ion-rich process streams using multi-stage osmotic separation
US10301198B2 (en) 2015-08-14 2019-05-28 Gradiant Corporation Selective retention of multivalent ions
US10308526B2 (en) 2015-02-11 2019-06-04 Gradiant Corporation Methods and systems for producing treated brines for desalination
US10308537B2 (en) 2013-09-23 2019-06-04 Gradiant Corporation Desalination systems and associated methods
US10518221B2 (en) 2015-07-29 2019-12-31 Gradiant Corporation Osmotic desalination methods and associated systems
US10689264B2 (en) 2016-02-22 2020-06-23 Gradiant Corporation Hybrid desalination systems and associated methods
CN112524902A (en) * 2020-12-09 2021-03-19 江西倍得力生物工程有限公司 Spray drying device is used in black-bone chicken peptide powder production
CN113039000A (en) * 2021-02-19 2021-06-25 安徽金禾实业股份有限公司 Production equipment and production method of sucrose-6-ester
CN113617046A (en) * 2021-06-25 2021-11-09 江苏京源环保股份有限公司 Magnetic force driven rotary atomizer
US11629072B2 (en) 2018-08-22 2023-04-18 Gradiant Corporation Liquid solution concentration system comprising isolated subsystem and related methods
US11667549B2 (en) 2020-11-17 2023-06-06 Gradiant Corporation Osmotic methods and systems involving energy recovery
US12023608B2 (en) 2016-01-22 2024-07-02 Gradiant Corporation Hybrid desalination systems and associated methods

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4243526A (en) * 1979-02-15 1981-01-06 Ransmark Sven Erik L Process for purifying liquids and a device for carrying out the process
FI61999C (en) * 1981-03-27 1982-11-10 Finn Aqua Ltd Oy DESTILLATIONSANORDNING SOM ARBETAR ENLIGT TERMOKOMPRESSORPRINCIPEN

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9969638B2 (en) 2013-08-05 2018-05-15 Gradiant Corporation Water treatment systems and associated methods
US10308537B2 (en) 2013-09-23 2019-06-04 Gradiant Corporation Desalination systems and associated methods
US10308526B2 (en) 2015-02-11 2019-06-04 Gradiant Corporation Methods and systems for producing treated brines for desalination
US10167218B2 (en) 2015-02-11 2019-01-01 Gradiant Corporation Production of ultra-high-density brines
US11400416B2 (en) 2015-07-29 2022-08-02 Gradiant Corporation Osmotic desalination methods and associated systems
US10518221B2 (en) 2015-07-29 2019-12-31 Gradiant Corporation Osmotic desalination methods and associated systems
US10301198B2 (en) 2015-08-14 2019-05-28 Gradiant Corporation Selective retention of multivalent ions
US10245555B2 (en) 2015-08-14 2019-04-02 Gradiant Corporation Production of multivalent ion-rich process streams using multi-stage osmotic separation
US12023608B2 (en) 2016-01-22 2024-07-02 Gradiant Corporation Hybrid desalination systems and associated methods
US10689264B2 (en) 2016-02-22 2020-06-23 Gradiant Corporation Hybrid desalination systems and associated methods
US11629072B2 (en) 2018-08-22 2023-04-18 Gradiant Corporation Liquid solution concentration system comprising isolated subsystem and related methods
US11667549B2 (en) 2020-11-17 2023-06-06 Gradiant Corporation Osmotic methods and systems involving energy recovery
CN112524902A (en) * 2020-12-09 2021-03-19 江西倍得力生物工程有限公司 Spray drying device is used in black-bone chicken peptide powder production
CN112524902B (en) * 2020-12-09 2021-12-28 江西倍得力生物工程有限公司 Spray drying device is used in black-bone chicken peptide powder production
CN113039000A (en) * 2021-02-19 2021-06-25 安徽金禾实业股份有限公司 Production equipment and production method of sucrose-6-ester
CN113039000B (en) * 2021-02-19 2022-11-04 安徽金禾实业股份有限公司 Production equipment and production method of sucrose-6-ester
CN113617046A (en) * 2021-06-25 2021-11-09 江苏京源环保股份有限公司 Magnetic force driven rotary atomizer

Also Published As

Publication number Publication date
DE1517363A1 (en) 1969-10-16
NL291327A (en)
NL6802024A (en) 1968-04-25
CH447056A (en) 1967-11-15

Similar Documents

Publication Publication Date Title
GB1013767A (en) Method and apparatus for purifying liquids
US3312600A (en) Heat-pump compressor type distillation apparatus for purifying water
US2798570A (en) Air conditioning
US3775993A (en) Art of evaporative cooling
US2852090A (en) Liquid type air conditioning apparatus and method for marine applications
GB1099470A (en) Improvements in or relating to the freezing of products
GB981630A (en) Producing fresh water from saline water
GB1133575A (en) Evaporation of liquid from solutions containing dissolved salts
US2557204A (en) Concentrating hygroscopic solution
US2276970A (en) Air conditioning system
US3311543A (en) Vapor compression still for distilling impure water
US3574066A (en) Multistage evaporation unit and gasliquid direct contact distillation apparatus
JPS5515632A (en) Dehumidifier
GB1466980A (en) Fluid-storage heat-exchangers particularly for heat recovery from vapour compression refrigeration systems
US2488116A (en) Refrigerator chamber cooled by evaporization of liquid by a current of air
GB1446348A (en) Air pollution control system for food processing apparatus
DK155297B (en) APPARATUS WITH COLD ROOMS FOR THE COOLING OF PREVENTABLE GOODS, ESPECIALLY FOOD
US1172429A (en) Method for dehumidifying and cooling air.
GB1246162A (en) Apparatus for generation of energy in a gas turbine cycle
US1142483A (en) Method of humidifying air.
US1987188A (en) Air conditioning system and method
JPS5750589A (en) Desalting method for salt-containing water of high temperature
US2443610A (en) Apparatus for drying with liquefied gas
US2094343A (en) Air conditioning
US1961686A (en) Material conditioning