GB1013767A - Method and apparatus for purifying liquids - Google Patents
Method and apparatus for purifying liquidsInfo
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/10—Treatment 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/02—Evaporators with heating coils
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/16—Evaporating by spraying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/007—Energy recuperation; Heat pumps
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/045—Treatment 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.
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)
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)
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 |
-
0
- NL NL291327D patent/NL291327A/xx unknown
-
1963
- 1963-04-04 GB GB1337663A patent/GB1013767A/en not_active Expired
- 1963-04-18 CH CH484563A patent/CH447056A/en unknown
-
1968
- 1968-02-13 NL NL6802024A patent/NL6802024A/xx unknown
-
1969
- 1969-10-15 DE DE19691517363 patent/DE1517363A1/en active Pending
Cited By (17)
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 |
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