WO2007148482A1 - プレート式造水装置 - Google Patents
プレート式造水装置 Download PDFInfo
- Publication number
- WO2007148482A1 WO2007148482A1 PCT/JP2007/059668 JP2007059668W WO2007148482A1 WO 2007148482 A1 WO2007148482 A1 WO 2007148482A1 JP 2007059668 W JP2007059668 W JP 2007059668W WO 2007148482 A1 WO2007148482 A1 WO 2007148482A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- water
- heat transfer
- plate
- heater
- heat
- Prior art date
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
- C02F1/048—Purification of waste water by evaporation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/22—Evaporating by bringing a thin layer of the liquid into contact with a heated surface
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
- B01D5/006—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with evaporation or distillation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
- F28B1/02—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using water or other liquid as the cooling medium
-
- 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
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
- F28D9/0043—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
- F28D9/005—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another the plates having openings therein for both heat-exchange media
-
- 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
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0093—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
-
- 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
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0061—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for phase-change applications
- F28D2021/0064—Vaporizers, e.g. evaporators
Definitions
- the present invention relates to a plate-type fresh water generator, and more particularly to a plate-type fresh water generator that performs evaporation of raw seawater and condensation of steam using a plate-type heat exchanger.
- the plate-type fresh water generator is configured to heat and evaporate the raw seawater introduced from the raw water inlet 53 with hot water used for cooling the marine engine, etc.
- the heater 50 to be discharged, the evaporator 60 for evaporating the droplets contained in the water vapor discharged from the heater 50, and the water vapor introduced from the evaporator 60 via the steam inlet 73 are condensed by cooling seawater.
- Each of the heater 50 and the condenser 70 is a plate heat exchanger, and is configured such that heat is exchanged between the high-temperature fluid and the low-temperature fluid flowing between the plurality of stacked heat transfer plates. It has been.
- the condenser 70 a part of the cooling seawater heated and discharged by heat exchange with the steam is introduced from the raw water inlet 53 of the heater 50 as raw seawater.
- Patent Document 1 Japanese Patent Laid-Open No. 9-299927
- the conventional plate-type water freshener described above does not have sufficient heat exchange efficiency between the raw seawater introduced into the heater 50 and the hot water, and consequently requires a large heat transfer area.
- the large heat transfer plate was invited.
- an object of the present invention is to provide a plate-type fresh water generator capable of achieving downsizing and low cost by efficiently heating and raising raw material seawater.
- a plate-type water freshener for achieving the above object is the raw seawater
- a heater that generates steam by heating with warm water; and a condenser that generates distilled water by cooling the generated steam with cooling water.
- the heater is laminated between two end plates.
- a plate-type fresh water generator comprising a plurality of heat transfer plates arranged and configured to exchange heat by alternately passing water steam and cooling water between adjacent heat transfer plates, Condenser power It is characterized by comprising preheating means for heating a part of the discharged cooling water and introducing it into the heater as raw seawater.
- a plate-type fresh water generator for achieving the above object includes a heater that heats raw seawater with warm water to generate steam, and the generated steam is used as cooling water.
- the condenser is provided with a plurality of heat transfer plates stacked between two end plates, and steam and cooling water are provided between adjacent heat transfer plates.
- the cooling water discharged from the other end plate cover is introduced into the heater as raw seawater.
- a plate-type water freshener for achieving the above object includes a heater that heats raw seawater with warm water to generate steam, and the generated steam is used as cooling water.
- a condenser for generating distilled water by cooling further, and the heater includes a plurality of heat transfer plates stacked between two end plates, and raw seawater and hot water between adjacent heat transfer plates The condenser is provided with a plurality of heat transfer plates stacked between two end plates, and steam and cooling water are provided between adjacent heat transfer plates.
- the heater introduces raw seawater from one of the end plates, performs heat exchange with the hot water through a part of the plurality of stacked heat transfer plates, The raw material seawater after replacement is further heat-exchanged with warm water through the remaining heat transfer plate, and the other end plate force is discharged.
- the condenser introduces cooling water from one of the end plates, and removes a part of the plurality of stacked heat transfer plates.
- the heat exchange with water steam is performed, and a part of the cooling water after the heat exchange is discharged by one end plate force, and the remaining cooling water is further heated with the steam through the remaining heat transfer plate.
- the cooling water discharged from the other end plate after being exchanged and discharged from the other end plate cover can be introduced into the heater as raw seawater.
- the plate type fresh water generator of the present invention it is possible to reduce the size and cost by efficiently heating the raw seawater.
- FIG. 1 is a schematic configuration diagram of a plate-type fresh water generator according to a first embodiment of the present invention.
- FIG. 2 is a perspective view of essential parts of a heater and a condenser in the plate-type fresh water generator shown in FIG. 1.
- FIG. 3 is a schematic configuration diagram of a plate-type fresh water generator according to a second embodiment of the present invention.
- FIG. 4 is a perspective view of a main part of the condenser in the plate type fresh water generator shown in FIG. 3.
- FIG. 5 is a schematic configuration diagram of a plate-type fresh water generator according to a third embodiment of the present invention.
- FIG. 6 is a perspective view of a main part of a heater in the plate-type fresh water generator shown in FIG.
- FIG. 7 is a schematic configuration diagram of a conventional plate-type fresh water generator.
- FIG. 1 is a schematic configuration diagram of a plate-type fresh water generator according to a first embodiment of the present invention.
- the plate-type fresh water generator la heats raw seawater to generate steam, an evaporator 20 that separates steam 'brine (concentrated seawater), and cools steam.
- a condenser 30 that generates distilled water, and is particularly preferably used as a marine desalination apparatus.
- the heater 10 includes a raw water inlet 11 and a water vapor 'brine outlet 12 for introducing and discharging raw seawater, and a hot water inlet 13 for introducing and discharging hot water such as jacket cooling water for marine engines, respectively. And a hot water discharge port 14.
- the raw material seawater introduced from the raw material water inlet 11 is heated and evaporated by the hot water introduced from the hot water inlet 13 and discharged from the steam * brine outlet 12.
- the evaporator 20 includes a heated raw water inlet 21 for introducing the heated raw seawater discharged from the steam 'brine outlet 12, a steam outlet 22 for discharging water vapor generated from the raw seawater, And a brine outlet 23 for discharging the remaining brine.
- the condenser 30 includes a steam inlet 31 for introducing steam discharged from the steam outlet 22, a distilled water outlet 32 for discharging distilled water obtained by cooling the steam, and cooling the steam. There are provided a cooling water inlet 33 and a cooling water outlet 34 for introducing and discharging cooling water, respectively. Cooling seawater is introduced into the cooling water inlet 33 as cooling water by the operation of the ejector pump 35, and a part of the seawater discharged from the cooling water outlet 34 is used as driving water for the water ejector 36. The other part is led to the raw water inlet 11 of the heater 10 and used as raw seawater, and the rest is discharged outboard.
- distilled water outlet 32 Discharge from distilled water outlet 32
- the distilled water to be discharged is led to a fresh water tank (not shown) by a distilled water pump 37.
- the vacuum of the evaporator 20 and the condenser 30 is maintained by being connected to the maximum negative pressure part of the water ejector 36 and sucking non-condensable gas.
- the heater 10 and the condenser 30 are provided with plate-type heat exchange, and the configuration thereof is the same as that of a conventional plate-type water generator.
- the heater 10 is configured by alternately stacking two types of heat transfer plates 103a and 103b between two end plates 101 and 102, respectively. The edges are connected by connecting rods 10a and 10a.
- Each of the heat transfer plates 103a and 103b is formed in a rectangular shape, and two raw water flow ports 104 and 105 that form a flow path for raw seawater and steam are arranged diagonally in the opposite direction.
- Two hot water circulation ports 106, 107 forming the flow path are arranged on the other diagonal
- Raw material water inlet 11, steam * brine outlet 12, hot water inlet 13 and hot water outlet 14 are all provided in one end plate 101, and are used in a plurality of heat transfer plates 103a and 103b.
- Each of the heat transfer plates 103a and 103b has a groove 108a and 108b formed on one surface, and the groove 108a of the heat transfer plate 103a communicates the two raw water flow ports 104 and 105 with each other.
- the two hot water circulation ports 106 and 107 are isolated, and the groove 108b of the heat transfer plate 103b isolates the two raw water circulation ports 104 and 105, while the two hot water circulation ports 106 and 107 are in communication.
- Adjacent heat transfer plates 103a and 103b are sealed by a gasket (not shown). In FIG.
- the flow path formed in the stacking direction of the heat transfer plates 103 a and 103 b indicates the portion communicating with the grooves 108 a and 108 b by a broken line, and is separated from the grooves 108 a and 108 b.
- the part shown is shown by a solid line.
- the raw seawater and hot water introduced from the raw water inlet 11 and the hot water inlet 13 pass through the groove 108a of the heat transfer plate 103a and the groove 108b of the heat transfer plate 103b. Since each flows, the raw seawater and hot water alternately pass between the adjacent heat transfer plates 103a and 103b when viewed in the stacking direction of the heat transfer plates 103a and 103b. The As a result, heat exchange is performed between the raw seawater and the hot water via the heat transfer plates 103a and 103b. The raw seawater and hot water after the heat exchange are discharged from the steam * brine outlet 12 and hot water outlet 14, respectively.
- the condenser 30 also has the same configuration as the heater 10, and a plurality of two types of heat transfer plates 113a and 113b are alternately stacked between the two end plates 111 and 112, respectively. The edges are connected by connecting rods 30a and 30a.
- Each of the heat transfer plates 113a and 113b is formed in a rectangular shape, and two distillation flow ports 114 and 115 forming a steam (or distilled water) flow path are arranged on opposite sides of the cooling water.
- Two cooling water flow ports 116 and 117 that form the flow path are arranged on the other diagonal.
- the steam inlet 31, the distilled water outlet 32, the cooling water inlet 33 and the cooling water outlet 34 are all provided in one end plate 111, and are connected to the plurality of heat transfer plates 113a and 113b.
- the flow path formed by the distillation flow port 114, the flow path formed by the distillation flow port 115, the flow path formed by the cooling water flow port 116, and the flow path formed by the cooling water flow port 117 Are connected to each other.
- Each of the heat transfer plates 113a and 113b has a groove 118a and 118b formed on one surface, and the groove 118a of the heat transfer plate 113a communicates the two distillation flow ports 114 and 115 with each other.
- the two cooling water circulation ports 116 and 117 are isolated, and the groove 118b of the heat transfer plate 113b isolates the two raw water circulation ports 114 and 115, while the two hot water circulation ports 116 and 1 17 communicate with each other.
- Adjacent heat transfer plates 113a and 113b are sealed with a gasket (not shown). In FIG.
- the flow path formed in the stacking direction of the heat transfer plates 113 a and 113 b indicates a portion communicating with the groove portions 118 a and 118 b by a broken line, and is separated from the groove portions 118 a and 118 b.
- the part shown is shown by a solid line.
- the steam and cooling water introduced from the steam inlet 31 and the cooling water inlet 33 are supplied to the groove 118a of the heat transfer plate 113a and the groove 118b of the heat transfer plate 1 13b. Therefore, when viewed in the stacking direction of the heat transfer plates 113a and 113b, steam and cooling water alternately pass between the adjacent heat transfer plates 113a and 113b. As a result, heat exchange is performed between the steam and the cooling water via the heat transfer plates 113a and 113b. Distilled water and cooling water generated after heat exchange are each discharged. It is discharged from the port 32 and the cooling water discharge port 34.
- the cooling water discharged from the cooling water discharge port 34 is heated by heat exchange with water vapor, and a part thereof is introduced into the heater 10 as raw seawater.
- This configuration is the same force as a conventional plate-type water desalination device. If this cooling water is directly introduced into the heater 10 as raw seawater, the temperature of the raw seawater is not sufficiently raised, and the temperature required for evaporation It takes a lot of heat transfer area in the heater 10 in order to increase the temperature. The present inventors have clarified that this is because a good heat transfer coefficient in which the flow rate of the raw seawater between the heat transfer plates 103a is very slow cannot be obtained.
- a preheating device is provided in order to increase the temperature of the raw seawater introduced into the heater 10 to near the evaporation temperature.
- a heat exchanger 40 is disposed between the cooling water discharge port 34 and the raw material water introduction port 11, and jacket cooling water introduced into the hot water introduction port 13 of the heater 10.
- the plate-type fresh water generator la of this embodiment a part of the cooling water discharged from the condenser 30 is heated in the heat exchanger ⁇ 40 and then introduced into the heater 10 as raw seawater. Therefore, the raw material seawater flowing along the heat transfer plate 103a of the heater 10 evaporates at an early stage, and heat exchange with the hot water flowing along the heat transfer plate 103b can be performed at high speed. Therefore, since the heat transfer coefficient in the heater 10 can be increased, the heater 10 can be reduced in size and cost can be reduced.
- the configuration of the heat exchanger 40 is not particularly limited.
- it can be a plate-type heat exchanger.
- the number of plates can be easily adjusted, so the preheating temperature of the raw seawater can be easily controlled, and the flow rate of the fluid can be increased, so that the heat exchange efficiency can be increased. Furthermore, there is an effect that it is difficult to block the flow path.
- FIG. 3 is a schematic configuration diagram of a plate-type fresh water generator according to a second embodiment of the present invention
- FIG. 4 is a perspective view of a main part of the condenser.
- the plate type water freshener lb of this embodiment is the first In the plate type water freshener la of the embodiment, instead of providing the heat exchanger 40, the condenser 30 is provided with a preheating portion of the raw seawater.
- the same components as those in the first embodiment shown in FIGS. 1 and 2 are denoted by the same reference numerals, and description thereof is omitted.
- the condenser 39 of the present embodiment includes f3 ⁇ 4 of the two adjacent heat transfer plates 113a and 113b.
- the partition plate 39ai is provided with distillation circulation ports 114, 115 and a cooling water circulation port 116, while it has a cooling water circulation port 117 through which the introduced cooling water passes. Absent.
- the other end plate 112 is a raw material communicating with the cooling water inlet 33 through the cooling water circulation ports 116 and 117 of the heat transfer plates 113a and 113b and the cooling water circulation port 116 of the partition plate 39a.
- a seawater outlet 341 is formed.
- the cooling seawater introduced from the one end plate 111 via the cooling water introduction port 33 passes through a part of the stacked heat transfer plates 113a and 113b. Then, heat exchange with water vapor is performed, and a part of the cooling seawater after the heat exchange is discharged from one end plate 111 through the cooling water discharge port 34. The remaining portion of the cooled seawater after the heat exchange is again heat-exchanged with water vapor via the remaining portions of the stacked heat transfer plates 113a and 113b, and is discharged from the raw seawater discharge port 341 in the other end plate 112. The cooled seawater discharged from the raw seawater outlet 341 is introduced into the raw water inlet 11 of the heater 10 as shown in FIG.
- the condenser 39 in the plate-type fresh water generator lb of the present embodiment is configured such that after the cooling seawater discharged from the raw seawater discharge port 341 exchanges heat with steam, the partition plate 39a and the other Since the heat exchange with the steam is further performed between the end plate 112 and the end plate 112, the temperature is higher than that of the cooling seawater discharged from the condenser 30 shown in FIG. That is, in the condenser 39 of the present embodiment, since the partition plate 39a and the other end plate 112 constitute the preheating unit 41 that preheats the raw seawater introduced into the heater 10, The same effects as in the embodiment can be obtained.
- the temperature and flow rate of the cooling seawater discharged from the raw seawater discharge port 341 can be easily adjusted by appropriately selecting the insertion position of the partition plate 39a between the stacked heat transfer plates 113a and 113b. It is. That is, the insertion position force of the partition plate 39a
- the means for forming the above-described cooling water flow path is not necessarily limited to the configuration in which the partition plate 39a is provided.
- the cooling water circulation port 117 of the heat transfer plate 113a or 113b is used.
- Other configurations, such as a plug for closing, may be used.
- the condenser 39 of the present embodiment can be configured to include the preheating unit 41 by making a small improvement to the existing condenser, so that further miniaturization can be achieved, and heat exchange can be achieved. This is especially effective when there is a space limitation of ⁇ .
- the preheating unit 41 is a plate-type heat exchanger, the same effect as when the heat exchanger 40 in the first embodiment is a plate-type can be obtained.
- the effect of preventing blockage of the flow path is remarkable when the condenser 39 includes the preheating portion 41 as in the present embodiment.
- FIG. 5 is a schematic configuration diagram of a plate-type water freshener according to the third embodiment of the present invention
- FIG. 6 is a perspective view of a main part of the heater.
- the plate-type fresh water generator lc of the present embodiment is the same as the plate-type water freshener la of the first embodiment, except that the heat exchanger 40 is provided, and the heater 10 is provided with a preheating portion of raw seawater.
- the same components as those in the first embodiment shown in FIG. 1 and FIG. 2 are denoted by the same reference numerals, and the description thereof is omitted.
- the heater 19 of this embodiment includes a partition plate 19a between two adjacent heat transfer plates 103a and 103b.
- the partition plate 19a includes the raw water circulation port 104 and the hot water circulation ports 106 and 107, but does not include the raw water circulation port 105 through which the introduced raw seawater passes.
- the raw water inlet 11 is not provided in one end plate 101 but is provided in the other end plate 102.
- the raw water inlet 11 is a raw water distribution port of the heat transfer plates 103a and 103b.
- the raw seawater introduced from the other end plate 102 via the raw water introduction port 11 passes through a part of the laminated heat transfer plates 103a and 103b. After exchanging heat with warm water, the raw material seawater part after the heat exchange is further heat exchanged through the remaining heat transfer plates 103a, 103b and discharged from one end plate 111 through the steam 'brine outlet 12 Is done.
- the raw seawater introduced from the other end plate 102 exchanges heat with warm water between the partition plate 19a and the other end plate 102. Further, since the heat exchange with the hot water is performed, the preheating section 42 for preheating the raw seawater is formed between the partition plate 19a and the other end plate 102. Therefore, the plate type water freshener lc of the present embodiment can also achieve the same effects as those of the first embodiment.
- the temperature of the raw seawater that passes through the raw water circulation port 104 of the partition plate 19a can be easily adjusted by appropriately selecting the insertion position of the partition plate 19a between the heat transfer plates 103a and 103b that are stacked in large numbers. Is possible. That is, as the insertion position force of the partition plate 19a moves from the other end plate 102 side to the one end plate 101 side, the temperature of the raw seawater passing through the raw water circulation port 104 of the partition plate 19a increases.
- the means for forming the raw material seawater flow path described above is not necessarily limited to the configuration in which the partition plate 19a is provided.
- the raw water distribution port of the heat transfer plate 103a or 103b Other configurations, such as providing a plug to close 105, may be used.
- the heater 19 of the present embodiment can be configured to include the preheating unit 42 by making a small improvement to the existing heater, so that further downsizing can be achieved, and the heat exchange ⁇ This is especially effective when there are installation space constraints.
- the preheating unit 42 is a plate-type heat exchanger, the same effect as in the case where the heat exchange in the first embodiment is a plate-type can be obtained. Further, in the plate type water freshener lc of this embodiment, the configuration of the condenser 30 is changed to the configuration of the condenser 39 in the second embodiment shown in FIG. By configuring the raw seawater discharged from 341 to be introduced into the heater 19, further downsizing and high efficiency can be achieved.
Abstract
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2007800233156A CN101479195B (zh) | 2006-06-20 | 2007-05-10 | 板式造水装置 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2006169517A JP5132091B2 (ja) | 2006-06-20 | 2006-06-20 | プレート式造水装置 |
JP2006-169517 | 2006-06-20 |
Publications (1)
Publication Number | Publication Date |
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WO2007148482A1 true WO2007148482A1 (ja) | 2007-12-27 |
Family
ID=38833225
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/JP2007/059668 WO2007148482A1 (ja) | 2006-06-20 | 2007-05-10 | プレート式造水装置 |
Country Status (5)
Country | Link |
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JP (1) | JP5132091B2 (ja) |
KR (2) | KR20120034818A (ja) |
CN (1) | CN101479195B (ja) |
TW (1) | TWI413617B (ja) |
WO (1) | WO2007148482A1 (ja) |
Cited By (3)
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CN102259941A (zh) * | 2011-06-16 | 2011-11-30 | 大连理工大学 | 一种竖管喷涌沸腾海水蒸发器 |
CN101734739B (zh) * | 2008-11-20 | 2012-07-04 | 中国神华能源股份有限公司 | 海水淡化蒸发器凝结水排出装置 |
US20130043118A1 (en) * | 2011-08-19 | 2013-02-21 | WaterPointe-Global, LLC | Methods and Apparatus for Purifying Liquid Using Regenerating Heat Exchange |
Families Citing this family (9)
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KR101110733B1 (ko) * | 2008-09-17 | 2012-02-15 | 삼성중공업 주식회사 | 조수기의 열원 공급 장치 |
KR101051467B1 (ko) * | 2009-09-28 | 2011-07-25 | 주식회사 우건이엔지 | 증류수 냉각용 열교환장치 |
JP5603756B2 (ja) * | 2010-11-24 | 2014-10-08 | マツイマシン株式会社 | 蒸留塔及びその組立方法 |
JP5672450B2 (ja) * | 2011-02-25 | 2015-02-18 | 株式会社ササクラ | 造水装置および造水方法 |
JP5979395B2 (ja) * | 2014-11-11 | 2016-08-24 | 株式会社ササクラ | 造水装置および造水方法 |
FR3035710B1 (fr) * | 2015-04-29 | 2018-09-07 | Carrier Corporation | Echangeur thermique a plaques et machine frigorifique reversible comprenant un tel echangeur |
TWI757508B (zh) * | 2017-08-02 | 2022-03-11 | 日商笹倉機械工程股份有限公司 | 造水裝置 |
EP3734209A1 (en) * | 2019-04-30 | 2020-11-04 | Alfa Laval Corporate AB | A plate heat exchanger for treatment of a feed, a plate for a plate heat exchanger for treatment of a feed, a gasket for use together with the heat exchanger plate and a method of producing a heat exchanger for treatment of a feed |
JP7431447B2 (ja) | 2020-06-08 | 2024-02-15 | 株式会社東洋製作所 | 蒸留水製造装置 |
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JPS5194474A (ja) * | 1975-02-19 | 1976-08-19 | ||
JPH09299927A (ja) * | 1996-05-14 | 1997-11-25 | Sasakura Eng Co Ltd | プレート式造水装置 |
JPH10288480A (ja) * | 1997-04-15 | 1998-10-27 | Daikin Ind Ltd | プレート式熱交換器 |
JP2000283668A (ja) * | 1999-03-30 | 2000-10-13 | Ebara Corp | プレート式熱交換器及びそれを用いた溶液熱交換器 |
JP2003106782A (ja) * | 2001-09-28 | 2003-04-09 | Hisaka Works Ltd | 溶接型プレート式熱交換器 |
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US4409959A (en) * | 1981-04-30 | 1983-10-18 | Chevron Research Company | Solar energy water preheat system |
JP4400857B2 (ja) * | 2003-06-17 | 2010-01-20 | 株式会社ササクラ | プレート式造水装置 |
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2006
- 2006-06-20 JP JP2006169517A patent/JP5132091B2/ja active Active
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2007
- 2007-05-10 WO PCT/JP2007/059668 patent/WO2007148482A1/ja active Application Filing
- 2007-05-10 KR KR1020127005148A patent/KR20120034818A/ko not_active Application Discontinuation
- 2007-05-10 CN CN2007800233156A patent/CN101479195B/zh active Active
- 2007-05-10 KR KR1020087031663A patent/KR20090027676A/ko not_active Application Discontinuation
- 2007-05-16 TW TW96117349A patent/TWI413617B/zh active
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101734739B (zh) * | 2008-11-20 | 2012-07-04 | 中国神华能源股份有限公司 | 海水淡化蒸发器凝结水排出装置 |
CN102259941A (zh) * | 2011-06-16 | 2011-11-30 | 大连理工大学 | 一种竖管喷涌沸腾海水蒸发器 |
US20130043118A1 (en) * | 2011-08-19 | 2013-02-21 | WaterPointe-Global, LLC | Methods and Apparatus for Purifying Liquid Using Regenerating Heat Exchange |
US9211482B2 (en) * | 2011-08-19 | 2015-12-15 | Waterpointe—Global, LLC | Methods and apparatus for purifying liquid using regenerating heat exchange |
Also Published As
Publication number | Publication date |
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JP2008000636A (ja) | 2008-01-10 |
KR20090027676A (ko) | 2009-03-17 |
JP5132091B2 (ja) | 2013-01-30 |
CN101479195B (zh) | 2012-02-01 |
CN101479195A (zh) | 2009-07-08 |
KR20120034818A (ko) | 2012-04-12 |
TWI413617B (zh) | 2013-11-01 |
TW200800807A (en) | 2008-01-01 |
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