GB1235760A - Heat transfer - Google Patents
Heat transferInfo
- Publication number
- GB1235760A GB1235760A GB57712/68A GB5771268A GB1235760A GB 1235760 A GB1235760 A GB 1235760A GB 57712/68 A GB57712/68 A GB 57712/68A GB 5771268 A GB5771268 A GB 5771268A GB 1235760 A GB1235760 A GB 1235760A
- Authority
- GB
- United Kingdom
- Prior art keywords
- water
- flash
- withdrawn
- outlet
- column
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 9
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 abstract 5
- 239000011780 sodium chloride Substances 0.000 abstract 5
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 abstract 4
- 239000012267 brine Substances 0.000 abstract 2
- 235000011132 calcium sulphate Nutrition 0.000 abstract 2
- 239000001175 calcium sulphate Substances 0.000 abstract 2
- 238000010438 heat treatment Methods 0.000 abstract 2
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 abstract 2
- 238000001704 evaporation Methods 0.000 abstract 1
- 230000008020 evaporation Effects 0.000 abstract 1
- 238000007701 flash-distillation Methods 0.000 abstract 1
- 238000002347 injection Methods 0.000 abstract 1
- 239000007924 injection Substances 0.000 abstract 1
- 150000003839 salts Chemical class 0.000 abstract 1
- 239000013535 sea water Substances 0.000 abstract 1
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
- C02F1/06—Flash evaporation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
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)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
1,235,760. Heating saline water; flash-distillation plant. MONTECATINI EDISON S.p.A. 5 Dec., 1968 [6 Dec., 1967; 12 Nov., 1968], No. 57712/68. Heading B1B. Saline water, such as sea water, flows down column 10 (Fig. 1) and up column 11 which is heated at the base e.g. by injection of steam at 14; successive evaporation of some of the water takes place as the saline water rises up column 11, and the vapours collect under plates 17 and pass through apertures 13 into column 10 where the vapours condense in the downflowing saline water thereby heating it so that salts such as calcium sulphate are precipitated and can be withdrawn through outlet 22. Softened water is collected in vessel 7 which is at a lower level than vessel 6 so that the flow of water takes place by pressure difference. Air is withdrawn from the apparatus by ejector 8. The two columns may be arranged at concentric tubes. Fig. 6 shows a plant wherein a heat-transfer apparatus 30 of the type specified above is associated with a multi-stage flash evaporator comprising one flash section B at high temperature, a heater 31 and two flash sections A and C at low temperature. Saline water is introduced into the plant through inlet a; and desalinated water, which is collected in condensate trays below coils 32, 36, 37, is withdrawn through outlet c. Calcium sulphate is discharged through outlet d. Brine is withdrawn through outlet b; some of this brine is discharged and the remainder is recycled to the flash sections by pump 35. Fig. 7 (not shown) illustrates a multi-stage flash evaporator associated with a heat-transfer apparatus comprising two units (30') and (30").
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| IT2360467 | 1967-12-06 | ||
| IT2361768 | 1968-11-12 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1235760A true GB1235760A (en) | 1971-06-16 |
Family
ID=26328403
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB57712/68A Expired GB1235760A (en) | 1967-12-06 | 1968-12-05 | Heat transfer |
Country Status (8)
| Country | Link |
|---|---|
| BE (1) | BE724995A (en) |
| BR (1) | BR6804636D0 (en) |
| DE (1) | DE1812240A1 (en) |
| ES (2) | ES361040A1 (en) |
| FR (1) | FR1599889A (en) |
| GB (1) | GB1235760A (en) |
| IL (1) | IL31208A0 (en) |
| NL (1) | NL6817235A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20150190730A1 (en) * | 2013-09-12 | 2015-07-09 | Gradiant Corporation | Systems including a condensing apparatus such as a bubble column condenser |
| US10143936B2 (en) | 2015-05-21 | 2018-12-04 | Gradiant Corporation | Systems including an apparatus comprising both a humidification region and a dehumidification region with heat recovery and/or intermediate injection |
| US10143935B2 (en) | 2015-05-21 | 2018-12-04 | Gradiant Corporation | Systems including an apparatus comprising both a humidification region and a dehumidification region |
| US10294123B2 (en) | 2016-05-20 | 2019-05-21 | Gradiant Corporation | Humidification-dehumidification systems and methods at low top brine temperatures |
| US10463985B2 (en) | 2015-05-21 | 2019-11-05 | Gradiant Corporation | Mobile humidification-dehumidification desalination systems and methods |
| US10513445B2 (en) | 2016-05-20 | 2019-12-24 | Gradiant Corporation | Control system and method for multiple parallel desalination systems |
| US10981082B2 (en) | 2015-05-21 | 2021-04-20 | Gradiant Corporation | Humidification-dehumidification desalination systems and methods |
| US12023608B2 (en) | 2016-01-22 | 2024-07-02 | Gradiant Corporation | Hybrid desalination systems and associated methods |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4234391A (en) * | 1978-10-13 | 1980-11-18 | University Of Utah | Continuous distillation apparatus and method |
-
1968
- 1968-12-02 NL NL6817235A patent/NL6817235A/xx unknown
- 1968-12-03 IL IL31208A patent/IL31208A0/en unknown
- 1968-12-03 DE DE19681812240 patent/DE1812240A1/en active Pending
- 1968-12-04 FR FR1599889D patent/FR1599889A/fr not_active Expired
- 1968-12-04 ES ES361040A patent/ES361040A1/en not_active Expired
- 1968-12-05 BE BE724995D patent/BE724995A/xx unknown
- 1968-12-05 BR BR204636/68A patent/BR6804636D0/en unknown
- 1968-12-05 GB GB57712/68A patent/GB1235760A/en not_active Expired
-
1970
- 1970-04-30 ES ES379207A patent/ES379207A1/en not_active Expired
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20150190730A1 (en) * | 2013-09-12 | 2015-07-09 | Gradiant Corporation | Systems including a condensing apparatus such as a bubble column condenser |
| US9700811B2 (en) * | 2013-09-12 | 2017-07-11 | Gradiant Corporation | Systems including a condensing apparatus such as a bubble column condenser |
| US10286335B2 (en) | 2013-09-12 | 2019-05-14 | Gradiant Corporation | Systems including a condensing apparatus such as a bubble column condenser |
| US10143936B2 (en) | 2015-05-21 | 2018-12-04 | Gradiant Corporation | Systems including an apparatus comprising both a humidification region and a dehumidification region with heat recovery and/or intermediate injection |
| US10143935B2 (en) | 2015-05-21 | 2018-12-04 | Gradiant Corporation | Systems including an apparatus comprising both a humidification region and a dehumidification region |
| US10463985B2 (en) | 2015-05-21 | 2019-11-05 | Gradiant Corporation | Mobile humidification-dehumidification desalination systems and methods |
| US10981082B2 (en) | 2015-05-21 | 2021-04-20 | Gradiant Corporation | Humidification-dehumidification desalination systems and methods |
| US12023608B2 (en) | 2016-01-22 | 2024-07-02 | Gradiant Corporation | Hybrid desalination systems and associated methods |
| US10294123B2 (en) | 2016-05-20 | 2019-05-21 | Gradiant Corporation | Humidification-dehumidification systems and methods at low top brine temperatures |
| US10513445B2 (en) | 2016-05-20 | 2019-12-24 | Gradiant Corporation | Control system and method for multiple parallel desalination systems |
Also Published As
| Publication number | Publication date |
|---|---|
| ES361040A1 (en) | 1970-10-16 |
| IL31208A0 (en) | 1969-02-27 |
| NL6817235A (en) | 1969-06-10 |
| BE724995A (en) | 1969-06-05 |
| BR6804636D0 (en) | 1973-02-08 |
| DE1812240A1 (en) | 1970-02-19 |
| ES379207A1 (en) | 1972-09-01 |
| FR1599889A (en) | 1970-07-20 |
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