CN203999020U - A kind of multi-effect distilling solar energy sea water desalination apparatus that uses oscillating heat pipe - Google Patents
A kind of multi-effect distilling solar energy sea water desalination apparatus that uses oscillating heat pipe Download PDFInfo
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- CN203999020U CN203999020U CN201420360271.3U CN201420360271U CN203999020U CN 203999020 U CN203999020 U CN 203999020U CN 201420360271 U CN201420360271 U CN 201420360271U CN 203999020 U CN203999020 U CN 203999020U
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- solar energy
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- fresh water
- heat pipe
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- 239000013535 sea water Substances 0.000 title claims abstract description 65
- 238000010612 desalination reaction Methods 0.000 title claims abstract description 35
- 239000013505 freshwater Substances 0.000 claims abstract description 56
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 56
- 238000004821 distillation Methods 0.000 claims abstract description 23
- 238000011033 desalting Methods 0.000 claims abstract description 10
- 238000004891 communication Methods 0.000 claims abstract description 3
- 239000012267 brine Substances 0.000 claims description 8
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 8
- 238000009833 condensation Methods 0.000 claims description 5
- 230000005494 condensation Effects 0.000 claims description 5
- 229910001220 stainless steel Inorganic materials 0.000 claims description 5
- 239000010935 stainless steel Substances 0.000 claims description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 description 12
- 238000010438 heat treatment Methods 0.000 description 11
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 238000001816 cooling Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 238000003287 bathing Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000005068 transpiration Effects 0.000 description 1
Classifications
-
- 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
- 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
- Y02A20/138—Water desalination using renewable energy
- Y02A20/142—Solar thermal; Photovoltaics
-
- 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
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
A kind of multi-effect distilling solar energy sea water desalination apparatus that uses oscillating heat pipe, comprise desalting equipment and solar energy collector, desalting equipment comprises a casing, in casing, be provided with from top to bottom condensing heat-exchange face, fresh water collecting conduit and with the oscillating heat pipe of dividing plate, condensing heat-exchange face and dividing plate will be divided into three spaces in casing, between condensing heat-exchange face and case top, it is seawater preheating passage, it between condensing heat-exchange face and dividing plate, is sea water by distillation chamber, it between at the bottom of dividing plate and case, is high temperature fresh water passage, the entrance of high temperature fresh water passage on casing connects the water outlet of high-order high temperature fresh water tank and the water outlet of solar energy collector, outlet connects water outlet and the water-in of solar energy collector, the water outlet of fresh water tank connects the water-in of solar energy collector, sea water by distillation chamber and seawater preheating passage are by being arranged on the pipeline communication outside casing, the utility model provides night on daytime two kinds of operation scheme, has that water production rate is higher, simple in structure, energy consumption is low and advantages of environment protection.
Description
Technical field
The utility model belongs to hot method desalination with Solar Energy field, particularly a kind of multi-effect distilling solar energy sea water desalination apparatus that uses oscillating heat pipe.
Background technology
Hot method desalination with Solar Energy is divided into active and passive type.The heat heating seawater that passive type solar energy desalination technology relies on sun power to produce completely, does not rely on extra utility appliance, but completes passively sea water desaltination.The features such as this device has simple in structure, and operation expense is low, but maximum defect is that water production rate is not high, and the efficiency of current comparatively ideal disc type solar energy sea water desalinating plant is less than 40% also.Passive type heat and mass engineering is mainly natural convection relatively, the additional equipment that improves operating temperature of active solar energy sea water desalinating plant configuration, thereby improve the process of internal heat transfer mass transfer, its producing water ratio exceeds several times compared with passive type, and therefore active desalination technology has obtained using widely.Day by day universal along with middle low-temperature solar energy heat collector (flat, electron tubes type, trough type solar heat-collector, linear Fresnel formula solar energy collector etc.) application simultaneously, temperature section becomes possibility the desalination with Solar Energy of 75 ℃, therefore sun power is substituted to traditional fossil energy and combines and will have larger promotion prospect with conventional desalination technology.
Hot French desalination technology mainly comprises multistage flash evaporation; multi-effect distilling and vapour compression etc.; conventional desalination technology all has larger advantage compared with desalination with Solar Energy at aspects such as capacity usage ratio, water production rate, mass-producing and industrialization, thus desalination with Solar Energy is combined with conventional desalination technology be after the developing direction of desalination with Solar Energy.Sun power is combined and is mainly utilized solar energy collector to collect efficiently sun power with conventional desalination technology, thereby substitutes traditional fossil energy heating seawater.
Oscillating heat pipe is a kind of new and effective heat transfer element, except thering is conventional heat pipe, self also exist, shape low without wick, operation and maintenance cost arbitrarily under crooked, arbitrary angle all effectively work and evaporator section cooling section the peculiar strong point such as choose arbitrarily, but still lack a kind of technology that hot pipe technique, solar seawater desalination, conventional desalination technology three are combined at present.The disadvantageous effects such as generally, existing desalination with Solar Energy still exists the deficiencies such as the coefficient of heat transfer is little, energy consumption is low, concentration ratio is large, water production rate is less, and conventional sea water desaltination exists Fossil fuel consumption, contaminate environment.
Summary of the invention
In order to overcome the shortcoming of above-mentioned prior art, the purpose of this utility model is to provide a kind of multi-effect distilling solar energy sea water desalination apparatus that uses oscillating heat pipe, has that water production rate is higher, daytime and all can move night, simple in structure, energy consumption is low and advantages of environment protection.
To achieve these goals, the technical solution adopted in the utility model is:
A kind of multi-effect distilling solar energy sea water desalination apparatus that uses oscillating heat pipe, comprise desalting equipment and solar energy collector 9, described desalting equipment comprises a casing, in casing, be provided with from top to bottom condensing heat-exchange face 5, fresh water collecting conduit 6 and with the oscillating heat pipe 11 of dividing plate, condensing heat-exchange face 5 and dividing plate will be divided into three spaces in casing, between condensing heat-exchange face 5 and case top, it is seawater preheating passage 7, it between condensing heat-exchange face 5 and dividing plate, is sea water by distillation chamber 4, it between at the bottom of dividing plate and case, is high temperature fresh water passage 3, the entrance of described high temperature fresh water passage 3 on casing connects the water outlet of high-order high temperature fresh water tank 203 and the water outlet of solar energy collector 9 by pipeline, outlet connects water outlet and the water-in of solar energy collector 9 by pipeline, the outlet of described sea water by distillation chamber 4 on casing connects strong brine tank 201 by pipeline, described fresh water collecting conduit 6 connects fresh water tank 202 by pipeline, the water outlet of fresh water tank 202 connects the water-in of solar energy collector 9 by pipeline, sea water by distillation chamber 4 and seawater preheating passage 7 are by being arranged on the pipeline communication outside casing.
11 one-tenth loop structures of described oscillating heat pipe, tubing is copper or stainless steel, and intraductal working medium is highly purified distilled water, ammonia, methyl alcohol or the ethanol etc. compatible with tubing, in pipe, is evacuated, and vacuum tightness is 10
-2～10
-4pa.
The part that described oscillating heat pipe 11 is positioned at dividing plate top is condensation segment 1101, and condensation segment 1101 is worked in sea water by distillation chamber 4, and the part that is positioned at dividing plate below is evaporator section 1102, and evaporator section 1102 is worked in high temperature fresh water passage 3.
Described sea water by distillation chamber 4 is connected with vacuum pump 10, vacuum pump 10 effects are extracting seawater stilling chamber 4 air, and passage is reduced pressure, and this is because the realization of multi-effect distilling, the working pressure of a necessary rear effect sea water by distillation chamber is lower than last effect, thereby has heat transfer temperature difference.
Described solar energy collector 9 is flat, electron tubes type, slot type or linear Fresnel formula solar energy collector.
Described fresh water tank 202 and high-order high temperature fresh water tank 203 are shaped as vertical column or horizontal column.
Described condensing heat-exchange face 5 be shaped as wavy stainless steel materials, object is farthest to increase condensing heat-exchange area, transpiration cooling after heating of seawater in sea water by distillation chamber on the one hand, carries out preheating to the seawater of the system of entering on the other hand.Fresh water collecting conduit 6 cross-sectional shapes are V-type or U-shaped.
The water outlet of described solar energy collector 9 arranges the 7th valve 107, on the water outlet connecting tube of the entrance of high temperature fresh water passage 3 on casing and high-order high temperature fresh water tank 203, the 6th valve 106 is set, with on the water outlet connecting tube of solar energy collector 9, the 5th valve 105 is set, the water outlet of solar energy collector 9 is connected by pipeline with the water inlet of high-order high temperature fresh water tank 203 and the 4th valve 104 is set on pipeline, on the water outlet connecting tube of the outlet of high temperature fresh water passage 3 on casing and solar energy collector 9, the second valve 102 is set, with on the water-in connecting tube of solar energy collector 9, water circulating pump 8 is set, the 3rd valve 103 is set on the water-in connecting tube of the water outlet of described fresh water tank 202 and solar energy collector 9, on the connecting tube of the outlet of described sea water by distillation chamber 4 on casing and strong brine tank 201, the first valve 101 is set.
Described desalting equipment has a plurality of, serial setting.
Compared with prior art, the utility model combines oscillating heat pipe, solar energy collector and conventional desalination technology multi-effect distilling three, take full advantage of the superior heat transfer property of oscillating heat pipe, adopt solar energy collector both can avoid the consumption of fossil oil, utilize inexhaustible solar energy resources simultaneously, make native system have environmental protection and energy saving advantage, multi-effect distilling is conventional desalination technology, has less energy-consumption, larger loading elasticity and heat transfer effect etc. preferably.System described in the utility model not only can be moved daytime, and can also continue to move certain hour night, therefore have good economy.
Accompanying drawing explanation
Fig. 1 is the multi-effect distilling solar seawater desalination system schematic diagram of a kind of oscillating heat pipe of the utility model.
Fig. 2 is the oscillating heat pipe schematic diagram that system described in the utility model is used.
Embodiment
Below in conjunction with drawings and Examples, describe embodiment of the present utility model in detail.
As shown in Figure 1, a kind of multi-effect distilling solar energy sea water desalination apparatus that uses oscillating heat pipe, comprise desalting equipment and solar energy collector 9, desalting equipment comprises a casing, in casing, be provided with from top to bottom condensing heat-exchange face 5, fresh water collecting conduit 6 and with the oscillating heat pipe 11 of dividing plate, condensing heat-exchange face 5 and dividing plate will be divided into three spaces in casing, between condensing heat-exchange face 5 and case top, it is seawater preheating passage 7, between condensing heat-exchange face 5 and dividing plate, for sea water by distillation chamber 4, be high temperature fresh water passage 3 between at the bottom of dividing plate and case.The water outlet of solar energy collector 9 arranges the 7th valve 107, on the water outlet connecting tube of the entrance of high temperature fresh water passage 3 on casing and high-order high temperature fresh water tank 203, the 6th valve 106 is set, with on the water outlet connecting tube of solar energy collector 9, the 5th valve 105 is set, the water outlet of solar energy collector 9 is connected by pipeline with the water inlet of high-order high temperature fresh water tank 203 and the 4th valve 104 is set on pipeline, on the water outlet connecting tube of the outlet of high temperature fresh water passage 3 on casing and solar energy collector 9, the second valve 102 is set, with on the water-in connecting tube of solar energy collector 9, water circulating pump 8 is set, the 3rd valve 103 is set on the water-in connecting tube of the water outlet of fresh water tank 202 and solar energy collector 9, on the connecting tube of the outlet of sea water by distillation chamber 4 on casing and strong brine tank 201, the first valve 101 is set.
11 one-tenth loop structures of oscillating heat pipe, tubing is copper or stainless steel, and intraductal working medium is highly purified distilled water, ammonia, methyl alcohol or the ethanol etc. compatible with tubing, and liquid filled ratio is 50%, and 12 of elbow numbers are evacuated in pipe, and vacuum tightness is 10
-3pa.
According to above structure, the utility model provides following two kinds of operation scheme:
(1) daytime operating scheme:
Close the second valve 102 and the 6th valve 106, all the other valves are all opened, the seawater seawater preheating passage 7 of flowing through flows to sea water by distillation chamber 4, and fresh water is heated to after working temperature by solar energy collector 9, flow to high temperature fresh water passage 3, thereby the evaporator section 1102 of heating oscillating heat pipe 11, in heating pipe in vacuum state working medium be heated, generate liquid, plunger between vapour phase, cold, between hot junction, form larger pressure reduction, because vapour-liquid plunger is interspersed, thereby the strong reciprocating vibration motion of generation in pipe, working medium is delivered to cooling section 1101 efficiently by heat.
The seawater of sea water by distillation chamber 4 is by cooling section 1101 heating evaporations of oscillating heat pipe 11, thereby steam becomes condensed water to flow to fresh water tank 202 by fresh water collecting conduit 6 with condensing heat-exchange face 5 condensations by contact, and the seawater after evaporation flows to strong brine tank 201.Condensing heat-exchange face 5 is condensed steam on the one hand, the seawater that on the other hand can preheating flows to seawater preheating passage 7, the fresh water that fresh water tank is 202 li is leaded up to water circulating pump 8 and is pumped into high-order high-temperature water tank 203 and do insulation and store, and the high temperature fresh water of high-order high-temperature water tank 203 can be thermal source and the domestic hot-water who heats oscillating heat pipe 11 night.Another road of the fresh water that fresh water tank is 202 li is continued to flow to solar energy collector 9 heating and is flow to high temperature fresh water passage 3 heating Heat Pipes heats and efficiently transmit, and continues to impel sea water by distillation, and the strong brine flowing through behind sea water by distillation chamber 4 finally flows to strong brine tank 201.
(2) night operating scheme:
Night without solar radiation after, open the first valve 101, the second valve 102, the 5th valve 105 and the 6th valve 106, all the other valves are all closed.Be incubated the hot water of the high-order high-temperature water tank 203 having stored daytime, flow to the evaporator section 1102 of high temperature fresh water passage 3 heating oscillating heat pipes 11, working medium in vacuum state in heating pipe is delivered to cooling section 1101 efficiently by heat, and the heating seawater evaporating cold condensed water of congealing into flows to fresh water tank 202.Till moving the suitable bathing temperature of water temperature of duration with high-order high-temperature water tank 203 night.The start-up temperature of oscillating heat pipe 11 is 30 ℃ of left and right, and sea water desaltination temperature can realize seawater low temperature multiple-effect distillation 70 ℃ of left and right.Therefore the water tank of 203 li of high-order high-temperature water tanks is remained on to 90 ℃～100 ℃, thereby has the temperature difference of the left and right of 30 ℃ can make system described in the utility model continue operation for some time at night.
The above; it is only preferably embodiment of the utility model; but protection domain of the present utility model is not limited to this; anyly be familiar with those skilled in the art in the technical scope that the utility model discloses; the variation that can expect easily or replacement, within all should being encompassed in protection domain of the present utility model.Therefore, protection domain of the present utility model should be as the criterion with the protection domain of claim.
Claims (9)
1. a multi-effect distilling solar energy sea water desalination apparatus that uses oscillating heat pipe, comprise desalting equipment and solar energy collector (9), it is characterized in that, described desalting equipment comprises a casing, in casing, be provided with from top to bottom condensing heat-exchange face (5), fresh water collecting conduit (6) and with the oscillating heat pipe (11) of dividing plate, condensing heat-exchange face (5) and dividing plate will be divided into three spaces in casing, between condensing heat-exchange face (5) and case top, be seawater preheating passage (7), it between condensing heat-exchange face (5) and dividing plate, is sea water by distillation chamber (4), it between at the bottom of dividing plate and case, is high temperature fresh water passage (3), the entrance of described high temperature fresh water passage (3) on casing connects the water outlet of high-order high temperature fresh water tank (203) and the water outlet of solar energy collector (9) by pipeline, outlet connects water outlet and the water-in of solar energy collector (9) by pipeline, the outlet of described sea water by distillation chamber (4) on casing connects strong brine tank (201) by pipeline, described fresh water collecting conduit (6) connects fresh water tank (202) by pipeline, the water outlet of fresh water tank (202) connects the water-in of solar energy collector (9) by pipeline, sea water by distillation chamber (4) and seawater preheating passage (7) are by being arranged on the pipeline communication outside casing.
2. the multi-effect distilling solar energy sea water desalination apparatus of use oscillating heat pipe according to claim 1, is characterized in that, described oscillating heat pipe (11) becomes loop structure, and tubing is copper or stainless steel, in pipe, is evacuated, and vacuum tightness is 10
-2～10
-4pa.
3. the multi-effect distilling solar energy sea water desalination apparatus of use oscillating heat pipe according to claim 1, it is characterized in that, the part that described oscillating heat pipe (11) is positioned at dividing plate top is condensation segment (1101), condensation segment (1101) is worked in sea water by distillation chamber (4), the part that is positioned at dividing plate below is evaporator section (1102), and evaporator section (1102) is worked in high temperature fresh water passage (3).
4. the multi-effect distilling solar energy sea water desalination apparatus of use oscillating heat pipe according to claim 1, is characterized in that, described sea water by distillation chamber (4) is connected with vacuum pump (10).
5. the multi-effect distilling solar energy sea water desalination apparatus of use oscillating heat pipe according to claim 1, is characterized in that, described solar energy collector (9) is flat, electron tubes type, slot type or linear Fresnel formula solar energy collector.
6. the multi-effect distilling solar energy sea water desalination apparatus of use oscillating heat pipe according to claim 1, is characterized in that, described fresh water tank (202) and high-order high temperature fresh water tank (203) are shaped as vertical column or horizontal column.
7. the multi-effect distilling solar energy sea water desalination apparatus of use oscillating heat pipe according to claim 1, it is characterized in that, described condensing heat-exchange face (5) be shaped as wavy stainless steel materials, fresh water collecting conduit (6) cross-sectional shape is V-type or U-shaped.
8. the multi-effect distilling solar energy sea water desalination apparatus of use oscillating heat pipe according to claim 1, it is characterized in that, the water outlet of described solar energy collector (9) arranges the 7th valve (107), on the water outlet connecting tube of the entrance of high temperature fresh water passage (3) on casing and high-order high temperature fresh water tank (203), the 6th valve (106) is set, with on the water outlet connecting tube of solar energy collector (9), the 5th valve (105) is set, the water outlet of solar energy collector (9) is connected by pipeline with the water inlet of high-order high temperature fresh water tank (203) and the 4th valve (104) is set on pipeline, on the water outlet connecting tube of the outlet of high temperature fresh water passage (3) on casing and solar energy collector (9), the second valve (102) is set, with on the water-in connecting tube of solar energy collector (9), water circulating pump (8) is set, the 3rd valve (103) is set on the water-in connecting tube of the water outlet of described fresh water tank (202) and solar energy collector (9), on the connecting tube of the outlet of described sea water by distillation chamber (4) on casing and strong brine tank (201), the first valve (101) is set.
9. the multi-effect distilling solar energy sea water desalination apparatus of use oscillating heat pipe according to claim 1, is characterized in that, described desalting equipment has a plurality of, serial setting.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420360271.3U CN203999020U (en) | 2014-07-01 | 2014-07-01 | A kind of multi-effect distilling solar energy sea water desalination apparatus that uses oscillating heat pipe |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420360271.3U CN203999020U (en) | 2014-07-01 | 2014-07-01 | A kind of multi-effect distilling solar energy sea water desalination apparatus that uses oscillating heat pipe |
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| Publication Number | Publication Date |
|---|---|
| CN203999020U true CN203999020U (en) | 2014-12-10 |
Family
ID=52039051
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420360271.3U Expired - Lifetime CN203999020U (en) | 2014-07-01 | 2014-07-01 | A kind of multi-effect distilling solar energy sea water desalination apparatus that uses oscillating heat pipe |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203999020U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104085935A (en) * | 2014-07-01 | 2014-10-08 | 中国华能集团清洁能源技术研究院有限公司 | Multiple-effect distillation solar seawater desalination system using oscillation heat tube |
| WO2019154813A1 (en) * | 2018-02-08 | 2019-08-15 | Desolenator B.V. | A method for obtaining distillate from non-potable water as well as a device for obtaining distillate from non-potable water |
-
2014
- 2014-07-01 CN CN201420360271.3U patent/CN203999020U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104085935A (en) * | 2014-07-01 | 2014-10-08 | 中国华能集团清洁能源技术研究院有限公司 | Multiple-effect distillation solar seawater desalination system using oscillation heat tube |
| WO2019154813A1 (en) * | 2018-02-08 | 2019-08-15 | Desolenator B.V. | A method for obtaining distillate from non-potable water as well as a device for obtaining distillate from non-potable water |
| NL2020402A (en) * | 2018-02-08 | 2019-08-22 | Desolenator B V | A method for obtaining distillate from non-potable water as well as a device for obtaining distillate from non-potable water |
| US11235985B2 (en) | 2018-02-08 | 2022-02-01 | Desolenator B.V. | Method for obtaining distillate from non-potable water as well as a device for obtaining distillate from non-potable water |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20141210 |
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| CX01 | Expiry of patent term |