CN102464343A - Device for atomizing seawater to make salt by utilizing natural resources and collecting distilled water - Google Patents
Device for atomizing seawater to make salt by utilizing natural resources and collecting distilled water Download PDFInfo
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- CN102464343A CN102464343A CN2011101640247A CN201110164024A CN102464343A CN 102464343 A CN102464343 A CN 102464343A CN 2011101640247 A CN2011101640247 A CN 2011101640247A CN 201110164024 A CN201110164024 A CN 201110164024A CN 102464343 A CN102464343 A CN 102464343A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 77
- 150000003839 salts Chemical class 0.000 title claims abstract description 52
- 239000013535 sea water Substances 0.000 title claims abstract description 19
- 239000012153 distilled water Substances 0.000 title abstract 6
- 238000004821 distillation Methods 0.000 claims description 18
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 239000006096 absorbing agent Substances 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 7
- 238000005507 spraying Methods 0.000 claims description 6
- 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
- 238000009833 condensation Methods 0.000 abstract description 7
- 230000005494 condensation Effects 0.000 abstract description 7
- 239000007921 spray Substances 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
- 238000000034 method Methods 0.000 description 10
- 238000010248 power generation Methods 0.000 description 4
- 230000000630 rising effect Effects 0.000 description 4
- 239000012535 impurity Chemical group 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000003595 mist Substances 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
- 238000010586 diagram Methods 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
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000005273 aeration 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
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 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
- 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
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- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
- Y02E10/46—Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/70—Wind energy
- Y02E10/72—Wind turbines with rotation axis in wind direction
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- 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
-
- 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
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
-
- 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
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
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- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The invention relates to a device for atomizing seawater to make salt by utilizing natural resources and collecting distilled water. The device for atomizing the seawater to make the salt by utilizing the natural resources and collecting the distilled water is characterized in that: a salt making facility is placed in a solar wind power station, a pneumatic impeller is arranged on the lower part of a wind drum of the wind power station, and the pneumatic impeller is connected to a centrifugal spray throwing disc; an arc-shaped wind eave is arranged on the upper part of the wind drum, and a plurality of arc-shaped condensation pieces and a horn-shaped guide cylinder are arranged below the wind eave; the pneumatic impeller drives the throwing disc to rotate quickly, the brine is atomized to remove moisture rapidly, and a salt-containing part falls into the brine pool; the evaporated moisture enters the wind drum together with the hot blast so as to synthesize updraft rapidly; after the airflow passes through the pneumatic impeller and a plurality of wind power generators, the airflow flows out of the wind drum; on the other hand, the external airflow flows through the wind eave, the flow speed is accelerated and the pressure intensity is reduced, so that the airflow, which flows out of the wind drum, is sucked and rises up so as to flow to the exterior from a gap between the condensation pieces, and a part of steam is in contact with the condensation pieces so as to be chilled and condensed to the distilled water. The device for atomizing the seawater to make the salt by utilizing the natural resources and collecting the distilled water provided by the invention has the advantages that the salt making efficiency is improved and the distilled water is collected.
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;
On air duct top one circular arc wind eaves is set, the wind eaves has multi-disc circular arc condensate film and tubaeform guide shell; Have the gap between the condensate film, the condensate film center is provided with circular hole, and concentric with guide shell; Guide shell, condensate film and wind eaves are connected with air duct through support bar in proper order, and have a distance apart between guide shell and the air duct; First radiator element is provided with the distillation ditch; The zero(ppm) water ditch communicates with the distillation tank through the zero(ppm) water outfall sewer;
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;
Salt manufacturing of the present invention is achieved in that with the method for collecting zero(ppm) water
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; Flow out air duct behind this air-flow process wind rotor and many aerogenerators; On the other hand, because extraneous air flow stream is crossed the wind eaves, flow velocity is accelerated; Pressure reduces, and the air-flow that flows out air duct is aspirated rising, the circular hole through guide shell and condensate film center; Flow to extraneous from the gap between the condensate film; Wherein a part of water vapour condensation by contact sheet is caught a cold, and condenses into water droplet and falls into the distillation ditch, drops in the distillation tank through the zero(ppm) water outfall sewer;
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, increase the moisture evaporation area, make moisture rapid evaporation in warm air; But make concentraing pond in rainy day and the also operation of no sunlight period, improved product salt efficient.
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 the water vapour retrieving arrangement that has used wind eaves, condensate film etc. to form, 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 diagrammatic cross-section 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 D partial enlarged view among Fig. 3.
Fig. 7 is the C partial enlarged view among Fig. 3.
Fig. 8 is the E partial enlarged view among Fig. 7
Fig. 9 is the three-dimensional view of Fig. 7.
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 that utilizes sun power to produce promotes wind turbine power generation.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 6)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; Moisture evaporated rises, and gets into air duct 2 with warm air, synthetic fast rise air-flow; This air-flow flows out air duct 2 through wind rotor 51 and many aerogenerators 3 backs.
Process zero(ppm) water in order to collect water vapour, the present invention is provided with a circular arc wind eaves 92 (see figure 7)s on air duct 2 tops, and the wind eaves has multi-disc circular arc condensate film 9 and tubaeform guide shell 93; Have the gap between the condensate film, the condensate film center is provided with circular hole 94, and concentric with guide shell 93; Because extraneous air flow stream is crossed wind eaves 92, flow velocity is accelerated, according to bernoulli principle; Pressure reduces; The air-flow of above-mentioned outflow air duct 2 is aspirated rising, and circular hole 94 (see figure 9)s through guide shell 93 and condensate film center flow to extraneous from the gap between the condensate film 9; Wherein a part of water vapour condensation by contact sheet is caught a cold, and condenses into zero(ppm) water.
Guide shell, condensate film and wind eaves are connected with air duct 2 through support bar 95 in proper order; And has a distance apart 98 between guide shell and the air duct; When aerification in the guide shell 93 can't be discharged fast, effusive air-flow can be discharged from distance apart 98 from air duct 2; First radiator element 91 is provided with distillation ditch 96; The zero(ppm) water ditch communicates with distillation tank 6 through zero(ppm) water outfall sewer 97; The zero(ppm) water that each condensate film condenses into falls into distillation ditch 96, flows in the distillation tank 6 through zero(ppm) water outfall sewer 97;
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, salt manufacturing of the present invention is achieved in that with the method for collecting zero(ppm) water
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 flows out air duct 2 through wind rotor 51 and many aerogenerators 3 backs; On the other hand, because extraneous air flow stream is crossed wind eaves 92, flow velocity is accelerated; Pressure reduces, and the air-flow that flows out air duct 2 is aspirated rising, the circular hole 94 through guide shell 93 and condensate film center; Flow to extraneous from the gap between the condensate film 9; Wherein a part of water vapour condensation by contact sheet is caught a cold, and condenses into water droplet and falls into distillation ditch 96, drops in the distillation tank 6 through zero(ppm) water outfall sewer 97;
Extraneous air gets in the booth from many blast inlets 10 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. one kind is utilized natural energy resources atomizing preparing salt by working up seawater and the device of collecting zero(ppm) water, and it 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;
On air duct top one circular arc wind eaves is set, the wind eaves has multi-disc circular arc condensate film and tubaeform guide shell; Have the gap between the condensate film, the condensate film center is provided with circular hole, and concentric with guide shell; Guide shell, condensate film and wind eaves are connected with air duct through support bar in proper order, and have a distance apart between guide shell and the air duct; First radiator element is provided with the distillation ditch; The zero(ppm) water ditch communicates with the distillation tank through the zero(ppm) water outfall sewer;
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 |
|---|---|---|---|
| CN201110164024.7A CN102464343B (en) | 2011-06-17 | 2011-06-17 | Device for atomizing seawater to make salt by utilizing natural resources and collecting distilled water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110164024.7A CN102464343B (en) | 2011-06-17 | 2011-06-17 | Device for atomizing seawater to make salt by utilizing natural resources and collecting distilled water |
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| CN102464343A true CN102464343A (en) | 2012-05-23 |
| CN102464343B CN102464343B (en) | 2014-08-20 |
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Cited By (3)
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| CN104548631A (en) * | 2015-01-31 | 2015-04-29 | 王绍伟 | Blade type atomizing device and semi-immersed type seawater atomizing evaporator with same |
| US11502322B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11502323B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
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|---|---|---|---|---|
| CN105883858B (en) * | 2016-04-07 | 2017-09-26 | 淄博市技师学院 | A kind of pneumatic atomized water spray is evaporated brine machine |
| US11855324B1 (en) | 2022-11-15 | 2023-12-26 | Rahul S. Nana | Reverse electrodialysis or pressure-retarded osmosis cell with heat pump |
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| CN104548631A (en) * | 2015-01-31 | 2015-04-29 | 王绍伟 | Blade type atomizing device and semi-immersed type seawater atomizing evaporator with same |
| US11502322B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11502323B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
| US11563229B1 (en) | 2022-05-09 | 2023-01-24 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11611099B1 (en) | 2022-05-09 | 2023-03-21 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
| US11699803B1 (en) | 2022-05-09 | 2023-07-11 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
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