US3735808A - Heat-exchanger for desalting sea water - Google Patents
Heat-exchanger for desalting sea water Download PDFInfo
- Publication number
- US3735808A US3735808A US00158826A US3735808DA US3735808A US 3735808 A US3735808 A US 3735808A US 00158826 A US00158826 A US 00158826A US 3735808D A US3735808D A US 3735808DA US 3735808 A US3735808 A US 3735808A
- Authority
- US
- United States
- Prior art keywords
- heat
- exchanger
- partition
- hollow member
- tubes
- 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 - Lifetime
Links
- 239000013535 sea water Substances 0.000 title description 5
- 238000011033 desalting Methods 0.000 title description 3
- 238000005192 partition Methods 0.000 claims description 5
- 239000004033 plastic Substances 0.000 claims description 4
- 229920003023 plastic Polymers 0.000 claims description 4
- 238000007789 sealing Methods 0.000 claims 2
- 230000000295 complement effect Effects 0.000 claims 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 abstract description 6
- 239000013505 freshwater Substances 0.000 abstract description 2
- 239000011780 sodium chloride Substances 0.000 abstract description 2
- 239000000463 material Substances 0.000 description 3
- 238000003466 welding Methods 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 239000000110 cooling liquid Substances 0.000 description 1
- 230000003467 diminishing effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- QEVHRUUCFGRFIF-MDEJGZGSSA-N reserpine Chemical compound O([C@H]1[C@@H]([C@H]([C@H]2C[C@@H]3C4=C(C5=CC=C(OC)C=C5N4)CCN3C[C@H]2C1)C(=O)OC)OC)C(=O)C1=CC(OC)=C(OC)C(OC)=C1 QEVHRUUCFGRFIF-MDEJGZGSSA-N 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
Images
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
-
- 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
- B01D3/06—Flash distillation
- B01D3/065—Multiple-effect flash distillation (more than two traps)
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/007—Auxiliary supports for elements
- F28F9/013—Auxiliary supports for elements for tubes or tube-assemblies
- F28F9/0131—Auxiliary supports for elements for tubes or tube-assemblies formed by plates
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2230/00—Sealing means
-
- 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
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S159/00—Concentrating evaporators
- Y10S159/42—Seals
Definitions
- ABSTRACT The heat-exchanger tubes of instantaneous evaporators for providing fresh water from saline formed into a unitary nest by transverse supports corresponding in position with the walls dividing off successive chambers of the evaporator and in shape with holes provided in those walls.
- a plurality of instantaneous expansion chambers are provided which are connected in series and which operate at decreasing pressures.
- evaporators are obtained by subdividing the space enclosed by an outer shell by means of vertical baffles which extend in the transverse direction of the shell.
- the saline solution under evaporation is caused to flow through the chambers in the direction of diminishing pressure through passages of a particular shape, known as mouths, provided in the baffles.
- the vapor formed condenses on nests of heatexchanger tubes which longitudinally traverse the entire length of the evaporator and the condensate is collected so that it cannot comein contact with the saline solution.
- the sea-water is pre-heated before being introduced into the chambers by causing it to pass as cooling liquid through heat-exchanger tubes.
- the object of the present invention is an improvement relating to instantaneous multiple expansion evaporators, the said improvement making it easily, economically and particularlyadvantageously possible to achieve a high degree of leakproofness between the various chambers of the evaporators themselves, avoiding the above-described drawbacks.
- the individual tubes are no longer each caused to traverse a corresponding hole provided for the purpose in the wall of the dividing baffle; instead, the entire nest of tubes is rendered rigid with a hollow cylinder which is then passed through a single hole provided in the separating baffle so that a high degree of tightness is achieved between the cylinder and the hole.
- Each tube of the nest is located in apertures predisposed in the circular walls of the cylinderand there-- fore rendered rigid with'the cylinder itself.
- the tubes are rendered rigid with the cylinder by means of a plastics material which fills the cavity inside the cylinder.
- plastics materials particularly useful for the purpose are the polyolefines such as polyethylene and poly-propylene, polypropylene being preferred.
- the diameter of such a cylinder is slightly greater than that of the nest of tubesand its height is a little greater than the thickness of the separating baffle.
- the tightness between one chamber and the next is considerably improved, so that in the interior there are more regular temperature and pressure levels and hence a greater efficiency in the multiple expansion instantaneous evaporators.
- this is influenced by the fact that the linear development of the zone of tightness of the cylinder is considerably less than the sum of the linear developments of the zones of tightness which be necessary for each tube of the nest if each tube were so applied directly to the baffle.
- the improvement which is achieved by the invention makes it possible to carry out this operation far more rapidly and easily in that the nest of tubes is withdrawn en bloc by a single series of operations without its being necessary to repeat the same operations every time for each tube in the nest.
- a greatly simplified form of implementing the improvement of the present invention as an alternative to the foregoing resides in welding the tubes into the holes in a single plate having edges smoothed so that when the said plate is subsequently fitted into the hole in the baffle, it is possible to achieve a high degree of leakproofness.
- the attached drawing shows a longitudinal section through a preferred embodiment of the improvement according to the present invention.
- a nest of tubes 1 passes between two subsequent chambers through the hole in the dividing baffle 4 through the agency of a cylinder 2 with which the tubes are rendered rigid by the plastics material 3 which fills the cavity in the cylinder.
- the cylinder 2 is shaped so that a high degree of leakproofness can be obtained in the proximity of the hole in the dividing baffle 4. In any case, complete tightness may be obtained by using a single annularly disposed seal or leakproofing system.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The heat-exchanger tubes of instantaneous evaporators for providing fresh water from saline formed into a unitary nest by transverse supports corresponding in position with the walls dividing off successive chambers of the evaporator and in shape with holes provided in those walls.
Description
llnited States Patent [191 Barba et al.
HEAT-EXCHANGER FOR DESALTING SEA WATER Inventors: Diego Barba; Giuseppe Liuzzo;
Giovanni Tagliaferri; Antonino Germana, all of Rome, Italy Assignee: Societa ltaliana Resine S.p.A.,
Milan, Italy Filed: July 1, 1971 Appl. No.: 158,826
Foreign Application Priority Data July I, 1970 Italy ..26846A/70 U.S. C1 ..l65/69, 202/173 Int. Cl. .L ..F28f 7/00 Field of Search ..l65/70, 75, 79, 5,
[451 May 29,1973
[56] References Cited UNITED STATES PATENTS 3,174,914 3/1965 Worthen et al .202 73 3,324,941 6/1967 Divers ..l65/178 X 3,632,481 2/1970 Hammond .....202/173 Primary Examiner-Charles J, Myhre Assistant Examiner-Theophil W. Streule, Jr.
Attorney-Sughruel Rothwell, Mion, Zinn & Macpeak [57] ABSTRACT The heat-exchanger tubes of instantaneous evaporators for providing fresh water from saline formed into a unitary nest by transverse supports corresponding in position with the walls dividing off successive chambers of the evaporator and in shape with holes provided in those walls.
2 Claims, 1 Drawing Figure HEAT-EXCHANGE]! FOR DESALTING SEA WATER evaporators.
In multiple expansion instantaneous evaporators, for a high evaporation efficiency, a plurality of instantaneous expansion chambers are provided which are connected in series and which operate at decreasing pressures.
Normally, such evaporators are obtained by subdividing the space enclosed by an outer shell by means of vertical baffles which extend in the transverse direction of the shell. The saline solution under evaporation is caused to flow through the chambers in the direction of diminishing pressure through passages of a particular shape, known as mouths, provided in the baffles.
The vapor formed condenses on nests of heatexchanger tubes which longitudinally traverse the entire length of the evaporator and the condensate is collected so that it cannot comein contact with the saline solution.
In order to ensure best results and for economy in the process, the sea-water is pre-heated before being introduced into the chambers by causing it to pass as cooling liquid through heat-exchanger tubes.
For a high efficiency of the apparatus of this type in the removal of salt from sea-water, it is particularly important to maintain the pre-fixed temperature and pressure curves in the plurality of chambers as far as possible unaltered for the period of time involved.
Now, for passage of the tubes through the plurality of chambers, it is necessary to have numerous holes provided in the baffles which sub-divide the evaporator. Their presence however results in changes in the temperature and pressure levels in the chambers since substantial quantities-of vapor pass from one chamber to another through theeccentric annular space between the dividing wall and the tube.
In particular, the passage of vapor between the various stages at different pressuresoccurs to a consider able extent the greater is the difference between the operative pressures of the stages and the greater the number of consecutive chambers operating at decreasing pressure.
In multiple chamber instantaneous evaporators, when it is found that, in the vapor generated at elevated pressure and condensed at lower pressure, there is a lessening of energy which produces a change in the thermal profiles of the evolving fluids and thus a drop in the efficiency of the apparatus.
In order to obviate these drawbacks, it is important to achieve a high degree of leakproofness between one stage and the next and particularly around the eccenvirtue of the large number of heat-exchanger tubes involved, there are a very large number of holes in the baffles, the fitting of seals is inconvenient and expensive and it is also extremely difficult to replace seals inside the nest of tubes when, as normally happens, they have become worn out due to ageing.
In addition, such systems complicate the maintenance of such instantaneous evaporators when the entire nest of heat-exchanger tubes must be withdrawn.
In fact, since extraction of theentire nest of tubes ne- -cessitates every time repetition of the same operations for each tube and since each tube, in order to be released from the aforesaid leakproofing systems requires long and difficult operations, it is obvious how important it is to have a highly simplified leakproofing system in order to enjoy easy and rapid withdrawal of the nest of tubes.
The object of the present invention is an improvement relating to instantaneous multiple expansion evaporators, the said improvement making it easily, economically and particularlyadvantageously possible to achieve a high degree of leakproofness between the various chambers of the evaporators themselves, avoiding the above-described drawbacks.
According to the said improvements, the individual tubes are no longer each caused to traverse a corresponding hole provided for the purpose in the wall of the dividing baffle; instead, the entire nest of tubes is rendered rigid with a hollow cylinder which is then passed through a single hole provided in the separating baffle so that a high degree of tightness is achieved between the cylinder and the hole. v
Each tube of the nest, is located in apertures predisposed in the circular walls of the cylinderand there-- fore rendered rigid with'the cylinder itself.
In the preferred embodiment of the present invention, the tubes are rendered rigid with the cylinder by means of a plastics material which fills the cavity inside the cylinder. Of the plastics materials, particularly useful for the purpose are the polyolefines such as polyethylene and poly-propylene, polypropylene being preferred.
The diameter of such a cylinder is slightly greater than that of the nest of tubesand its height is a little greater than the thickness of the separating baffle.
There are numerous advantages which derive from the improvement which is the object of the present invention.
In particular, the tightness between one chamber and the next is considerably improved, so that in the interior there are more regular temperature and pressure levels and hence a greater efficiency in the multiple expansion instantaneous evaporators. Above all, this is influenced by the fact that the linear development of the zone of tightness of the cylinder is considerably less than the sum of the linear developments of the zones of tightness which be necessary for each tube of the nest if each tube were so applied directly to the baffle.
Furthermore, when during maintenance operations it is necessary to withdraw the nest of tubes from the evaporators, the improvement which is achieved by the invention makes it possible to carry out this operation far more rapidly and easily in that the nest of tubes is withdrawn en bloc by a single series of operations without its being necessary to repeat the same operations every time for each tube in the nest.
A greatly simplified form of implementing the improvement of the present invention as an alternative to the foregoing resides in welding the tubes into the holes in a single plate having edges smoothed so that when the said plate is subsequently fitted into the hole in the baffle, it is possible to achieve a high degree of leakproofness.
In this latter case, in order to facilitate the welding operations which are carried out by means of processes normally used in welding of metallic surfaces, it is preferable to use elevated tube-bushings for the holes in the plate.
The attached drawing shows a longitudinal section through a preferred embodiment of the improvement according to the present invention.
A nest of tubes 1 passes between two subsequent chambers through the hole in the dividing baffle 4 through the agency of a cylinder 2 with which the tubes are rendered rigid by the plastics material 3 which fills the cavity in the cylinder.
The cylinder 2 is shaped so that a high degree of leakproofness can be obtained in the proximity of the hole in the dividing baffle 4. In any case, complete tightness may be obtained by using a single annularly disposed seal or leakproofing system.
It will be appreciated that while two particularly advantageous forms of transverse support for the nest of tubes have been described above, namely hollow cylinders and simple perforated plates, other suitable members can readily be devised by those skilled in the art.
What we claim is:
1. In a heat-exchanger of the type having a plurality I .filling said hollow member to seal the apertures through which said conduits extend.
2. In a heat-exchanger as set forth in claim 1 wherein said hollow member is a circular cylinder having a length only slightly greater than the thickness of said partition.
Claims (2)
1. In a heat-exchanger of the type having a plurality of heat exchanger conduits extending through at least one partition therein, a supporting and sealing arrangement for said conduits comprising a single aperture extending through said partition, a hollow member having an external configuration complementary to said aperture disposed in close fitting engagement in said aperture, said hollow member having a pair of spaced apart end walls parallel to said partition and a plurality of aligned apertures extending through said end walls, a plurality of conduits extending through said apertures in close fitting engagement and plastic sealing means filling said hollow member to seal the apertures through which said conduits extend.
2. In a heat-exchanger as set forth in claim 1 wherein said hollow member is a circular cylinder having a length only slightly greater than the thickness of said partition.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| IT2684670 | 1970-07-01 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3735808A true US3735808A (en) | 1973-05-29 |
Family
ID=11220357
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US00158826A Expired - Lifetime US3735808A (en) | 1970-07-01 | 1971-07-01 | Heat-exchanger for desalting sea water |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US3735808A (en) |
| JP (1) | JPS5227859Y2 (en) |
| CH (1) | CH525842A (en) |
| DE (1) | DE2132603A1 (en) |
| FR (1) | FR2098138A5 (en) |
| GB (1) | GB1304977A (en) |
| NL (1) | NL7109086A (en) |
| YU (1) | YU35841B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4004984A (en) * | 1975-02-07 | 1977-01-25 | Aktiebolaget Atomenergi | Distillation plant |
| CN108562173A (en) * | 2018-04-09 | 2018-09-21 | 江苏安邦电化有限公司 | Phosphorus trichloride condenser |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3323987A1 (en) * | 1983-07-02 | 1985-01-10 | Balcke-Dürr AG, 4030 Ratingen | MULTI-STAGE HEAT EXCHANGER |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3174914A (en) * | 1959-01-19 | 1965-03-23 | Bethlehem Steel Corp | Tandem flash distilling plant |
| US3324941A (en) * | 1964-01-02 | 1967-06-13 | Carrier Corp | Heat exchanger with expansible tube seal |
| US3632481A (en) * | 1970-02-13 | 1972-01-04 | Roland P Hammond | Critical velocity, uninterruptedly flowing brine in multistage distillation system |
-
1970
- 1970-06-30 YU YU1719/71A patent/YU35841B/en unknown
-
1971
- 1971-06-21 CH CH905371A patent/CH525842A/en not_active IP Right Cessation
- 1971-06-25 GB GB3002971A patent/GB1304977A/en not_active Expired
- 1971-06-30 FR FR7123995A patent/FR2098138A5/fr not_active Expired
- 1971-06-30 DE DE19712132603 patent/DE2132603A1/en active Pending
- 1971-07-01 US US00158826A patent/US3735808A/en not_active Expired - Lifetime
- 1971-07-01 NL NL7109086A patent/NL7109086A/xx unknown
-
1976
- 1976-08-10 JP JP1976106991U patent/JPS5227859Y2/ja not_active Expired
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3174914A (en) * | 1959-01-19 | 1965-03-23 | Bethlehem Steel Corp | Tandem flash distilling plant |
| US3324941A (en) * | 1964-01-02 | 1967-06-13 | Carrier Corp | Heat exchanger with expansible tube seal |
| US3632481A (en) * | 1970-02-13 | 1972-01-04 | Roland P Hammond | Critical velocity, uninterruptedly flowing brine in multistage distillation system |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4004984A (en) * | 1975-02-07 | 1977-01-25 | Aktiebolaget Atomenergi | Distillation plant |
| CN108562173A (en) * | 2018-04-09 | 2018-09-21 | 江苏安邦电化有限公司 | Phosphorus trichloride condenser |
| CN108562173B (en) * | 2018-04-09 | 2023-09-29 | 安道麦安邦(江苏)有限公司 | Phosphorus trichloride condenser |
Also Published As
| Publication number | Publication date |
|---|---|
| NL7109086A (en) | 1972-01-04 |
| JPS5233644U (en) | 1977-03-09 |
| YU35841B (en) | 1981-08-31 |
| JPS5227859Y2 (en) | 1977-06-24 |
| YU171971A (en) | 1981-02-28 |
| CH525842A (en) | 1972-07-31 |
| GB1304977A (en) | 1973-01-31 |
| DE2132603A1 (en) | 1972-01-05 |
| FR2098138A5 (en) | 1972-03-03 |
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