ES379207A1 - METHOD FOR THE EXCHANGE OF HEAT IN THE VAPOR PHASE BETWEEN LI-QUIDOS. - Google Patents

METHOD FOR THE EXCHANGE OF HEAT IN THE VAPOR PHASE BETWEEN LI-QUIDOS.

Info

Publication number
ES379207A1
ES379207A1 ES379207A ES379207A ES379207A1 ES 379207 A1 ES379207 A1 ES 379207A1 ES 379207 A ES379207 A ES 379207A ES 379207 A ES379207 A ES 379207A ES 379207 A1 ES379207 A1 ES 379207A1
Authority
ES
Spain
Prior art keywords
water
withdrawn
outlet
column
heat
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
ES379207A
Other languages
Spanish (es)
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.)
Montedison SpA
Original Assignee
Montedison SpA
Montecatini Edison SpA
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 Montedison SpA, Montecatini Edison SpA filed Critical Montedison SpA
Publication of ES379207A1 publication Critical patent/ES379207A1/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
    • C02F1/06Flash evaporation
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water 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

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").
ES379207A 1967-12-06 1970-04-30 METHOD FOR THE EXCHANGE OF HEAT IN THE VAPOR PHASE BETWEEN LI-QUIDOS. Expired ES379207A1 (en)

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
ES379207A1 true ES379207A1 (en) 1972-09-01

Family

ID=26328403

Family Applications (2)

Application Number Title Priority Date Filing Date
ES361040A Expired ES361040A1 (en) 1967-12-06 1968-12-04 Heat transfer
ES379207A Expired ES379207A1 (en) 1967-12-06 1970-04-30 METHOD FOR THE EXCHANGE OF HEAT IN THE VAPOR PHASE BETWEEN LI-QUIDOS.

Family Applications Before (1)

Application Number Title Priority Date Filing Date
ES361040A Expired ES361040A1 (en) 1967-12-06 1968-12-04 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)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4234391A (en) * 1978-10-13 1980-11-18 University Of Utah Continuous distillation apparatus and method
KR102424159B1 (en) 2013-09-12 2022-07-25 그라디언트 코포레이션 Systems including a condensing apparatus such as a bubble column condenser
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
US10143935B2 (en) 2015-05-21 2018-12-04 Gradiant Corporation Systems including an apparatus comprising both a humidification region and a dehumidification region
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
WO2017127607A1 (en) 2016-01-22 2017-07-27 Gradiant Corporation Formation of solid salts using high gas flow velocities in humidifiers, such as multi-stage bubble column humidifiers
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
FR1599889A (en) 1970-07-20
ES361040A1 (en) 1970-10-16
BE724995A (en) 1969-06-05
GB1235760A (en) 1971-06-16
BR6804636D0 (en) 1973-02-08
DE1812240A1 (en) 1970-02-19
NL6817235A (en) 1969-06-10
IL31208A0 (en) 1969-02-27

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