CN102464368A - Device for producing salt and distilled water by spraying with solar energy and wind power - Google Patents
Device for producing salt and distilled water by spraying with solar energy and wind power Download PDFInfo
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- CN102464368A CN102464368A CN2011101640196A CN201110164019A CN102464368A CN 102464368 A CN102464368 A CN 102464368A CN 2011101640196 A CN2011101640196 A CN 2011101640196A CN 201110164019 A CN201110164019 A CN 201110164019A CN 102464368 A CN102464368 A CN 102464368A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 73
- 150000003839 salts Chemical class 0.000 title claims abstract description 50
- 238000005507 spraying Methods 0.000 title claims abstract description 12
- 239000012153 distilled water Substances 0.000 title abstract 5
- 238000004519 manufacturing process Methods 0.000 claims abstract description 11
- 238000004821 distillation Methods 0.000 claims description 10
- 239000006096 absorbing agent Substances 0.000 claims description 9
- 239000000411 inducer Substances 0.000 claims description 8
- 239000002184 metal Substances 0.000 claims description 7
- 230000002093 peripheral effect Effects 0.000 claims description 4
- 239000012267 brine Substances 0.000 abstract description 13
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 abstract description 13
- 230000001174 ascending effect Effects 0.000 abstract 1
- 238000001704 evaporation Methods 0.000 description 31
- 230000008020 evaporation Effects 0.000 description 26
- 241001131796 Botaurus stellaris Species 0.000 description 13
- 239000013535 sea water Substances 0.000 description 13
- 238000000034 method Methods 0.000 description 9
- 238000010586 diagram Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000012535 impurity Chemical group 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000003595 mist Substances 0.000 description 3
- 238000010248 power generation Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 230000002269 spontaneous effect Effects 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000007738 vacuum evaporation Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Images
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
- Y02A20/138—Water desalination using renewable energy
- Y02A20/141—Wind power
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The invention relates to a device for producing salt and distilled water by spraying with solar energy and wind power. The device for producing salt and distilled water by spraying with the solar energy and the wind power is characterized in that a salt production facility is arranged in a solar-energy wind-power station and a pneumatic impeller connected with a centrifugal spraying projecting disk is arranged at the lower part of an air funnel of the solar-energy wind-power station; a condenser pipe is arranged outside the air funnel, a rotational air gathering cover is arranged at the upper part of the air funnel and communicated to inside of the condenser pipe, and an electric fan is arranged in the connected position where the air gather cover is connected with the condenser pipe; the pneumatic impeller drives the projecting disk to rotate quickly, brine is atomized to quickly remove water, and then salt-containing parts fall into a brine tank; the evaporated water enters into the air funnel together with hot air to form a rapidly ascending air flow; and the air flow slows down after flowing through the pneumatic impeller and multiple wind driven generators, the air flow flowing out of the air funnel flows into the air gathering cover and the condenser pipe under the actions of external wind power and the electric fan, and water vapor in the water flow is cooled on a flow deflector and the wall of the condenser pipe to be condensed to form distilled water which falls into a water receiving basin. According to the invention, salt production efficiency can be increased and distilled water can be recycled.
Description
Technical field
The invention belongs to the ecological engineering technology field, especially relate to a kind of device that utilizes natural energy resources to make salt and zero(ppm) water.
Background technology
The method of salt manufacturing is got salt by evaporation of sea-water, boil the salt off the water, sun power evaporation is evaporated brine, cold method, vacuum-evaporation and thermocompression evaporation etc.Evaporate brine except the sun power evaporation, remaining method nearly all will consume mass energy.Because to evaporate brine is to utilize sun power and wind energy transpiring moisture concentrated brine, so be traditional salt manufacturing mode of economy and environmental protection the most.Yet, adopted advanced spissated step by step method though evaporate brine at present, production efficiency is increased, but still be to rely on the spontaneous evaporation of the concentraing pond waters surface at different levels to make bittern concentration principle gradually.Its weak point is that moisture evaporation is slow, and rainy day and evening almost can not operations, and its inefficiency has seriously restricted the development of the enterprise of evaporating brine; And its moisture evaporated wastes, and is also regrettable.Explore the efficient salt-sunning method of a kind of solar wind-energy, overcome the tradition inefficient shortcoming of evaporating brine, and to collect moisture evaporated be zero(ppm) water that the development of evaporate brine enterprise's synergy and low-carbon economy is all had great promoter action.
Summary of the invention
The objective of the invention is to evaporating brine at present mainly is to utilize the spontaneous evaporation of the concentraing pond water surface; Inefficient problem, and the present situation that can not collect moisture evaporated propose a kind of like this salt making apparatus: first; Under the situation that does not change concentraing pond areas at different levels and non-consumes energy; Enlarge the area of moisture evaporation, increase the air temperature and current speed of transpiring moisture, improve the efficient of moisture evaporation.The second, collect the water vapour of evaporation and make zero(ppm) water.The 3rd, the solar thermal energy of storage can continue transpiring moisture salt manufacturing and make zero(ppm) water in rainy day and evening.
Main technical schemes of the present invention: the salt manufacturing facility is placed in the wind power station utilizing solar energy of prior art; Make full use of high, the fast characteristics of gas velocity of the interior AT of film booth in power house; With the bittern atomizing, quicken moisture evaporation and become zero(ppm) water with the recycle-water steam.
Concrete technique device of the present invention is achieved in that it comprises many aerogenerators in booth, air duct and the air duct of wind power station utilizing solar energy, is characterized in that the concentraing ponds at different levels of salt manufacturing place in the booth; In the air duct bottom at least one wind rotor is set, the wind rotor below connects a centrifugal spraying with axle and gets rid of dish; Get rid of dish top one water pump is set;
Air duct outer setting one prolong, both are concentric; Being provided with one on prolong top can be around the wind gathering cover of prolong axis rotation, and wind gathering cover is provided with the wind rudder; Wind gathering cover communicates with prolong inside, and is provided with a motor fan in the internal connection; The prolong bottom is provided with a water-accepting basin; Prolong inside is provided with many volution inducers, and the outside is provided with the multi-disc radiator element; Water-accepting basin links to each other with the distillation tank through water pipe;
The peripheral bottom of booth is provided with distillation tank and Yan Ku, is provided with the metal absorber plate of black in the salt storehouse; Booth and air duct junction are provided with the baffle plate of block water steam;
The method of the present invention's running is:
In concentraing pond, add seawater, solar radiation is advanced in the film booth, air in the booth and the Absorption by Sea Water solar heat in the concentraing pond; Generate water vapour and warm air and rise, it is cold that a part of water vapour wherein rises to the booth chance, condenses into water droplet; Inclined-plane along booth drops down, and falls into the distillation tank; Remaining water vapour and hot blast be to air duct, rises along air duct again, drives many wind turbine power generations and wind rotor rotation in the air duct;
Wind rotor drives centrifugal spraying and gets rid of the dish fast rotational; Water pump is transported to the bittern in the concentraing pond and gets rid of on the dish; Bittern is thrown away by the atwirl dish that gets rid of, and makes bittern be dispersed into the very thin particulate as mist, and warm air contacts with particulate; Moment is removed most moisture evaporation in the particulate, and remaining contains salt and impurity part and residual moisture and falls into concentraing pond;
Moisture evaporated rises, and gets into air duct with warm air, synthetic fast rise air-flow; This air-flow through wind rotor and many aerogenerators after flow velocity lower; The air-flow that flows out air duct is under the effect of extraneous wind-force and motor fan; Get in wind gathering cover and the prolong; Water vapour in the air-flow is met cold on volution inducer and prolong tube wall, condenses into zero(ppm) water, falls into water-accepting basin; All the other waste gas are overflowed from the condensation mouth of pipe on the water-accepting basin;
Extraneous air gets in the canopy from many blast inlets of booth;
Simultaneously, the ferrous metal absorber plate in the salt storehouse also absorbs solar radiant heat, and its heat conducts in salt, makes the salt store heat;
In the time period of no sunlight, the seawater release of heat in salt and the concentraing pond, the air in the heating booth, seawater continues evaporation, continues to produce zero(ppm) water; A part water vapour and warm air continue to flow to air duct, rise along air duct again, drive many wind turbine power generations and wind rotor rotation in the air duct;
Evaporate seawater so again and again, produce zero(ppm) water and generating, until seawater condensing crystal salify, the salt storehouse in this salt input canopy becomes heat accumulating.
The present invention's characteristics and beneficial effect compared with prior art is:
One, utilizes interior quick air-flow of wind power station utilizing solar energy booth and higher temperature and air duct; Make the bittern atomizing; Just increase the moisture evaporation area; Make moisture rapid evaporation in warm air, but make concentraing pond, improved product salt efficient in rainy day and the also operation of no sunlight period.
And the moisture of concentraing pond and salinity are than rock and earth thermal storage performance better material, help discharging heat energy in the no sunlight period, make the aerogenerator in the air duct continue generating, have improved generating efficiency.
Above-mentioned both complement each other, and have played mutual promoting action.
Two, owing to used the water vapour retrieving arrangement of compositions such as wind gathering cover, prolong and the booth of wind power station utilizing solar energy, make the water vapour of original waste be recovered as zero(ppm) water.
Three, salt is put in storage in booth nearby, and this good heat accumulating of salt is made the best use of everything, thereby when overcast and rainy and evening, the salt release of heat helps continuing transpiring moisture, produces zero(ppm) water and generating.And salt puts in storage nearby, reduced trucking costs.
Description of drawings
Below in conjunction with figure and embodiment the present invention is further specified.
Fig. 1 is the wind power station utilizing solar energy diagrammatic cross-section of prior art.
Fig. 2 is the A partial enlarged view among Fig. 1.
Fig. 3 is that the salt manufacturing facility is arranged on the synoptic diagram in the wind power station utilizing solar energy booth.
Fig. 4 is the B partial enlarged view among Fig. 3.
Fig. 5 is a monnolithic case synoptic diagram of the present invention.
Fig. 6 is the C partial enlarged view among Fig. 3.
Fig. 7 is the D partial enlarged view among Fig. 3.
Fig. 8 is the synoptic diagram that the volution inducer is set in the prolong.
Fig. 9 is the G partial enlarged view among Fig. 8.
Figure 10 is the profile synoptic diagram that inserts the metal absorber plate in the salt.
Embodiment
The efficient of evaporating brine is mainly by the decision of the speed of moisture evaporation, and the evaporation of moisture depends primarily on temperature, and gas velocity and evaporation area implement to improve the efficient of evaporating brine around these three factors below.
What Fig. 1 and Fig. 2 showed is wind power station utilizing solar energy of the prior art, and it is the device that a kind of hot gas flow pushing generator that utilizes sun power to produce generates electricity.Large-area transparent plastic film booth 1 is laid at the place at the power generation assembly place, and sunlight sees through film, is absorbed by ground in the canopy.When sunny, the air between film booth and the ground can be heated to 20-50 ℃, and the booth center has tower shape air duct 2, is shone in the air flow air duct 2 of heat, rises along air duct 2 again, drives many aerogenerators 3 in the air duct.Even extraneous wind-force is zero level, the gas velocity in the air duct also can reach 80 meter per seconds, is equivalent to the speed of hurricane.Power is 1000 kilowatts this power house, need to build 10 meters of diameters, high 300 meters air duct, and the diameter that covers the film booth on ground is 400 meters.
Higher temperature and flow velocity air-flow faster in this film booth and the canopy just in time is used for accelerating the moisture evaporation of concentraing ponds 4 at different levels.Particularly in the rainy day, booth plays the effect that hides rain.And the water vapour of evaporation can condense into water droplet on booth 1, drops down along the inclined-plane of booth, becomes zero(ppm) water.On the other hand, the thermal capacity of water is quite high, and 1kg water can store 4.19kJ/ ℃ heat energy, and solid ground is about 1.7 kJ/ ℃, has only about 4/10 of water.Salinity in the bittern is the good material of heat accumulation especially.In the time period of no sunlight, the heat that water and salinity store can provide the wind energy of generating conversely for the aerogenerator in the air duct 23.
Aspect the increase evaporation area: the present invention is provided with at least one wind rotor 51 (see figure 7)s in air duct 2 bottoms, and the wind rotor below connects a centrifugal spraying with axle 52 and gets rid of dish 53; Get rid of dish top one water pump 54 is set; Wind rotor drives centrifugal spraying and gets rid of dish fast rotational (can use the wheel box governing speed); Water pump is transported to the bittern in the concentraing pond 4 and gets rid of on the dish, and bittern is thrown away by the dish that gets rid of of high speed rotating, makes bittern be dispersed into the very thin particulate as mist; Just increase the moisture evaporation area; Warm air contacts with particulate, and moment is removed most moisture evaporation in the particulate, and remaining contains salt and impurity part and residual moisture and falls into concentraing pond;
Process zero(ppm) water in order to collect water vapour, the present invention is in air duct 2 outer setting one prolong 81 (see figure 3)s, and both are concentric; Being provided with one on prolong top can be around the wind gathering cover 82 of prolong axis rotation, and wind gathering cover is provided with wind rudder 83, makes the wind gathering cover mouth all the time in face of wind direction; Wind gathering cover communicates with prolong inside, and is provided with a motor fan 84 (see figure 6)s in the internal connection; Extraneous air-flow will be pressed in the wind gathering cover from the air-flow that the air duct mouth comes out, and by motor fan air-flow sucked in the prolong.Prolong inside is provided with many volution inducers 85 (seeing Fig. 8 and Fig. 9, for ease of understanding the volution of in Fig. 3, Fig. 6 and Fig. 7, not drawing inducer 85), and the outside is provided with multi-disc radiator element 86; Water vapour in the air-flow is met cold in volution inducer and prolong tube wall, condenses into zero(ppm) water, flows into the water-accepting basin 87 of prolong bottom; Water-accepting basin links to each other with distillation tank 6 through water pipe 88, so zero(ppm) water can flow in the distillation tank;
The peripheral bottom of (seeing Fig. 3 and Fig. 4) booth is provided with distillation tank 6, drops down the zero(ppm) water that comes from the inclined-plane of canopy and can flow in the distillation tank and store.
The peripheral bottom of booth is provided with salt storehouse 7; Because salt is the excellent material of store heat; But its heat conductivity a little less than, so the present invention is provided with the metal absorber plate 71 (seeing Fig. 4 and Figure 10) of black on salt, the metal absorber plate of black absorbs solar heat; Through its many heat conduction pin 72, spread heat is conducted to salt 73; In the time period of no sunlight, salt conducts heat to absorber plate 71 conversely, by absorber plate release of heat in booth.
The junction of booth and air duct is provided with the baffle plate 8 of block water steam; This is in order to let water vapour can have more opportunity to contact with booth, to produce zero(ppm) water.Otherwise water vapour can get in the air duct 2 very soon, wastes.On the other hand, water vapor condensation Cheng Shuihui emits latent heat, and a part of latent heat wherein can return in booth.Water will absorb vaporization heat when evaporation, can lose a part of temperature in the booth, but as long as suitably increase the area of booth, the area that perhaps dwindles concentraing pond is just passable.
In sum, the method for salt manufacturing of the present invention and generating is achieved in that
In concentraing pond 4, add seawater; Solar radiation is advanced in the film booth 1, and air in the booth and the Absorption by Sea Water solar heat in the concentraing pond generate water vapour and warm air and rise; A part of water vapour in the base rises to booth 1 and meets cold; Condense into water droplet, drop down, fall into distillation tank 6 along the inclined-plane of booth; Remaining water vapour and hot blast are in air duct 2, and again along rising in the air duct, 3 generatings of many aerogenerators and the wind rotor 51 that drive in the air duct rotate;
Moisture evaporated rises, and gets into air duct 2 with warm air, synthetic fast rise air-flow; This air-flow lowers through wind rotor 51 and many aerogenerators 3 back flow velocitys; The air-flow that flows out air duct 2 is under the effect of extraneous wind-force and motor fan 84; Get in wind gathering cover 82 and the prolong 81; Water vapour in the air-flow is met cold on volution inducer 85 and prolong 81 tube walls, condenses into zero(ppm) water, falls into water-accepting basin 87; All the other waste gas are overflowed from the condensation mouth of pipe on the water-accepting basin;
Extraneous air gets in the booth from many blast inlets 9 of booth;
Simultaneously, the ferrous metal absorber plate 71 on the salt storehouse also absorbs solar radiant heat, and its heat conducts in salt 73, makes the salt store heat;
In the time period of no sunlight, the seawater release of heat in salt and the concentraing pond, the air in the heating booth, seawater continues evaporation, continues to produce zero(ppm) water; Part water vapour and warm air continue to flow to air duct 2, rise along air duct again, and 3 generatings of many aerogenerators and the wind rotor 51 that drive in the air duct rotate;
Evaporate seawater so again and again, produce zero(ppm) water and generating, until seawater condensing crystal salify (prior art), the salt storehouse 7 in this salt input canopy becomes heat accumulating.If needs are arranged, then can be from the salt storehouse from exporting salt to the external world.
Claims (1)
1. device that utilizes solar wind force spraying to make salt and zero(ppm) water comprises many aerogenerators in booth, air duct and the air duct of wind power station utilizing solar energy, it is characterized in that the concentraing ponds at different levels of salt manufacturing place in the booth; In the air duct bottom at least one wind rotor is set, the wind rotor below connects a centrifugal spraying with axle and gets rid of dish; Get rid of dish top one water pump is set;
Air duct outer setting one prolong, both are concentric; Being provided with one on prolong top can be around the wind gathering cover of prolong axis rotation, and wind gathering cover is provided with the wind rudder; Wind gathering cover communicates with prolong inside, and is provided with a motor fan in the internal connection; The prolong bottom is provided with a water-accepting basin; Prolong inside is provided with many volution inducers, and the outside is provided with the multi-disc radiator element; Water-accepting basin links to each other with the distillation tank through water pipe;
The peripheral bottom of booth is provided with distillation tank and Yan Ku, is provided with the metal absorber plate of black in the salt storehouse; Booth and air duct junction are provided with the baffle plate of block water steam.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110164019.6A CN102464368B (en) | 2011-06-17 | 2011-06-17 | Device for producing salt and distilled water by spraying with solar energy and wind power |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110164019.6A CN102464368B (en) | 2011-06-17 | 2011-06-17 | Device for producing salt and distilled water by spraying with solar energy and wind power |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102464368A true CN102464368A (en) | 2012-05-23 |
| CN102464368B CN102464368B (en) | 2015-05-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110164019.6A Expired - Fee Related CN102464368B (en) | 2011-06-17 | 2011-06-17 | Device for producing salt and distilled water by spraying with solar energy and wind power |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102464368B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110410906A (en) * | 2019-07-29 | 2019-11-05 | 张凇源 | Wind power generation formula is sprayed radiator |
| CN115814447A (en) * | 2023-02-16 | 2023-03-21 | 南京杰亚挤出装备有限公司 | Polymer takes off and volatilizees equipment |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3222538A1 (en) * | 1982-06-16 | 1983-12-22 | Gerhard 7766 Gaienhofen Beil | Apparatus for desalting water, in particular seawater |
| DE10152702A1 (en) * | 2001-10-19 | 2003-11-20 | Wolfhart Freiherr Stackelberg | Method for evaporating sea-water or brackish water involves spraying of the water from above into a reactor and supplying the latter with solar-heated air in counter-flow from below |
| CN101481154A (en) * | 2009-02-16 | 2009-07-15 | 浙江大学 | Method and apparatus for seawater desalination by comprehensive utilization of solar energy |
| CN101671056A (en) * | 2009-10-14 | 2010-03-17 | 国家海洋局天津海水淡化与综合利用研究所 | Distillation desalination system and desalination method thereof for solar chimney |
| CN202072503U (en) * | 2011-06-17 | 2011-12-14 | 冯静 | Device for manufacturing salt and distilled water through solar energy and wind power spray |
-
2011
- 2011-06-17 CN CN201110164019.6A patent/CN102464368B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3222538A1 (en) * | 1982-06-16 | 1983-12-22 | Gerhard 7766 Gaienhofen Beil | Apparatus for desalting water, in particular seawater |
| DE10152702A1 (en) * | 2001-10-19 | 2003-11-20 | Wolfhart Freiherr Stackelberg | Method for evaporating sea-water or brackish water involves spraying of the water from above into a reactor and supplying the latter with solar-heated air in counter-flow from below |
| CN101481154A (en) * | 2009-02-16 | 2009-07-15 | 浙江大学 | Method and apparatus for seawater desalination by comprehensive utilization of solar energy |
| CN101671056A (en) * | 2009-10-14 | 2010-03-17 | 国家海洋局天津海水淡化与综合利用研究所 | Distillation desalination system and desalination method thereof for solar chimney |
| CN202072503U (en) * | 2011-06-17 | 2011-12-14 | 冯静 | Device for manufacturing salt and distilled water through solar energy and wind power spray |
Non-Patent Citations (1)
| Title |
|---|
| 朱丽: "结合水力发电利用太阳能烟囱技术强化海水淡化初探", 《天津大学学报》, vol. 39, no. 5, 31 December 2006 (2006-12-31), pages 575 - 580 * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110410906A (en) * | 2019-07-29 | 2019-11-05 | 张凇源 | Wind power generation formula is sprayed radiator |
| CN110410906B (en) * | 2019-07-29 | 2021-04-09 | 张凇源 | Wind power generation type spray heat dissipation device |
| CN115814447A (en) * | 2023-02-16 | 2023-03-21 | 南京杰亚挤出装备有限公司 | Polymer takes off and volatilizees equipment |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102464368B (en) | 2015-05-13 |
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