CN204849897U - Superconductive strong effect water extraction from air machine - Google Patents
Superconductive strong effect water extraction from air machine Download PDFInfo
- Publication number
- CN204849897U CN204849897U CN201520172741.8U CN201520172741U CN204849897U CN 204849897 U CN204849897 U CN 204849897U CN 201520172741 U CN201520172741 U CN 201520172741U CN 204849897 U CN204849897 U CN 204849897U
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- Prior art keywords
- water
- air
- superconductive
- heat exchanger
- superconducting
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- 230000000694 effects Effects 0.000 title abstract 2
- 238000003809 water extraction Methods 0.000 title abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 62
- 230000006835 compression Effects 0.000 claims abstract description 14
- 238000007906 compression Methods 0.000 claims abstract description 14
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000013505 freshwater Substances 0.000 claims abstract description 3
- 229910052782 aluminium Inorganic materials 0.000 claims abstract 2
- 238000000746 purification Methods 0.000 claims description 6
- 150000003839 salts Chemical class 0.000 claims description 6
- 238000003860 storage Methods 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 2
- 238000005086 pumping Methods 0.000 claims description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 claims 1
- 239000011707 mineral Substances 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 13
- 239000013535 sea water Substances 0.000 abstract description 11
- 239000002887 superconductor Substances 0.000 abstract description 8
- 239000011435 rock Substances 0.000 abstract description 6
- 150000001450 anions Chemical class 0.000 abstract description 5
- 206010037660 Pyrexia Diseases 0.000 abstract 1
- 150000001875 compounds Chemical class 0.000 abstract 1
- 230000000737 periodic effect Effects 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 9
- 230000003389 potentiating effect Effects 0.000 description 9
- 238000009833 condensation Methods 0.000 description 8
- 230000005494 condensation Effects 0.000 description 8
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 5
- 238000001704 evaporation Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 239000012528 membrane Substances 0.000 description 4
- 108010066278 cabin-4 Proteins 0.000 description 3
- 230000007812 deficiency Effects 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000033558 biomineral tissue development Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000000249 desinfective effect Effects 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000010327 methods by industry Methods 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000007634 remodeling Methods 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
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- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model discloses a superconductive strong effect water extraction from air machine, this technique is by the water pump, send into the sea water between the high -temperature superconductor evaporimeter in the sealed steam drum, the evaporimeter boils through the height is warm, produce a large amount of steams, pass through the pipeline, pump in the indoor air compression heat exchanger in mobilizable solar energy cabin, inhale the compound compression, superconductive condenser periodic duty, adsorb the moisture content moisture content in the air on the aluminum sheet, produce a large amount of water droplets promptly, in the inflow cistern, and carry out anion ore deposit rock and filter the water treatment, thereby the shortage of fresh water has been improved.
Description
Technical field
The utility model relates to a kind of device for fetching water from air, particularly relates to the potent air water intaking device of a kind of superconduction.
Background technology
Current, mainly contain the research of air water-intaking problem both at home and abroad: the companies such as the U.S., Australia, Singapore and Qingdao Ao Kema, the difference of its research level is mainly reflected in process two aspects with water of producing of water; 1. water produce at present, air water-intaking technology is divided into two large classes: separating and condensing method and dew condensation method.No matter adopt separating and condensing method and dew condensation fanal kind mode, all need that cooling is carried out to air and analyse wet; 2. the external drinking water advanced treatment skill of the process recent year of water ... (checking more) art aspect achieves greater advance, and the water technology as air condensed water mainly contains: active carbon adsorption technology, ozone disinfecting technology, membrane technology; Reverse osmosis membrane RO, NF membrane NF, milipore filter UF, microfiltration membranes MF or Ultraviolet Disinfection.
The domestic and international research for air water-intaking at present mainly also concentrates on the theory and technology aspect of condensation water making, absorption type water, solar energy and semiconductor water etc., manufacture theory being used for product is still immature, is especially wanting also rare in the applicabilities such as cube is little, water outlet is low.For this reason, in the utility model, the research of producing of water has certain reliability, aquifer yield and water treatment three aspect from system cloud gray model emphatically, utilize the quick absorption system device of seawater steam humidification, be this in conjunction with solar energy power program, concentrate the technical method of water source purifying process engineering, reach the form of the scientific purified treatment of high flow capacity water outlet, select have in the environment of certain humidity on sea, relative humidity in air is artificially increased and carries out air water-intaking, be transported to this practicality technology that the series of processes of water is carried out in large-scale water storage storehouse.
This device strengthens relative humidity, optimize and revise cold and hot utilization, achieve uninterrupted continuous flow water, ensure that the safe for drinking of water quality, achieve highly effective sea-water humidification method air water-intaking, technical advanced person is feasible, solve the problem of Island insufficient water, there is wide market prospects and good economic benefit.
Summary of the invention
The utility model is used for the potent air water intaking device of superconduction and includes: sealed steam tank, moveable solar machine cabin, high-temperature superconductor evaporimeter, suction pump, heat of compression interchanger, fan, water containing pool, output channel and control cabinet, purification pot, store salt cellar and efficiency natural anion ore deposit rock strainer composition.
By water pump, seawater is sent between the high-temperature superconductor evaporimeter in sealed steam tank, evaporimeter is boiled by high-temperature hot, produce a large amount of water vapours, by pipeline, pump in the air compressing heat interchanger in moveable solar machine cabin, carry out inhaling multiple condensation compression work, moisture content in air is adsorbed on aluminium flake, namely produces a large amount of water droplets, flow in reservoir.
For this reason, the technical problems to be solved in the utility model is to provide a kind of circulating system, by water pump 9 seawater 8 sent between the high-temperature superconductor evaporimeter 2 in sealed steam tank 1, evaporimeter 2 is boiled by high-temperature hot, produce a large amount of water vapours, by pipeline 7, pump in the air compressing heat interchanger 5 in room, moveable solar energy 3 cabin 4, carry out inhaling multiple condensation compression work, moisture content in air is adsorbed on aluminium flake, namely a large amount of water droplets is produced, flow in reservoir 6, use the potent air water intaking device of superconduction, humidity intensity can be promoted rapidly, add the practicality of adsorption of large equipment.
When normal boot-strap → seawater 8 is heated by high-temperature superconductor evaporimeter 2 after, evaporation forms the water vapour of strong humidity → suck condensation compression heat radiation from air intake by the pumping of pipeline 7 → moist steam, moisture content in air to be adsorbed on aluminium flake → vapor can 1 forms water droplet → flow out fresh-water pool 6 from output channel 7 constantly entering humidity → process compression heat exchanger 5, so move in circles, thus overcome above-mentioned prior art not enough, water yield is few, evaporates slow time factor.
To be extracted in purification pot 10 by water pump 9 according to the reservoir 6 in the utility model figure and carry out the rock filtered water process of anion ore deposit, reduce turbidity of sea water, prevent the microbial growth such as bacterium, algae, TDS content from 36000 mg/litre, be down to 200 mg/litre, utilize natural negative ion ore deposit rock and medical stone, trace element is added to water, high fluorine low mineralization bitter Saltwater Sea Water warfare is reached drinkable standard water.
The described sodium chloride be left behind at evaporation of seawater can obtain crude salt 11; For what contain in removing crude salt
sO 4 2- ,
ca 2+ ,
mg 2+ deng impurity, must carry out dissolving, adding quantitatively
na 2 cO 3 solution, add quantitative
baCl 2 solution, add quantitative hydrochloric acid, add quantitatively
naOHsolution, evaporative crystallization multiprogrammable filtration.
Above-mentioned technology is used for the usability of the potent air water intaking device of superconduction, can overcome the deficiency existing for aforementioned prior art, and because this facility adopts the photovoltaic energy, control system can be selected arbitrarily to connect.
Accompanying drawing explanation
Below in conjunction with embodiment and accompanying drawing, describe the character of the potent air water intaking device of the utility model superconduction in detail.
Fig. 1 is the potent air water intaking device branch figure of the utility model superconduction.
Detailed description of the invention
In FIG, the technical problems to be solved in the utility model is to provide a kind of circulating system, by water pump 9 seawater 8 sent between the high-temperature superconductor evaporimeter 2 in sealed steam tank 1, evaporimeter 2 is boiled by high-temperature hot, produce a large amount of water vapours, by pipeline 7, pump in the air compressing heat interchanger 5 in room, moveable solar energy 3 cabin 4, carry out inhaling the work of multiple condensation compression cycle, moisture content in air is adsorbed on aluminium flake, namely produce a large amount of water droplets and flow into reservoir 6, so move in circles, thus overcome the deficiency of above-mentioned prior art, water yield is few, evaporate slow time factor.
The potent air water intaking device of superconduction includes: sealed steam tank 1, moveable room, solar energy 3 cabin 4, high-temperature superconductor evaporimeter 2, suction pump 9, heat of compression interchanger 5, fan, water containing pool 6, output channel 7 and control cabinet, purification pot 10, store salt cellar 11, efficiency natural anion ore deposit rock strainer 10 forms.
To be extracted in purification pot 10 by water pump 9 according to the reservoir 6 in the utility model figure and carry out the rock filtered water process of anion ore deposit.
The described sodium chloride be left behind at evaporation of seawater can obtain the recycling of crude salt 11.
The beneficial effects of the utility model are under any environment having relative humidity, use the series of tasks principle extracting the condensation of humidity air circulation Compression Evaporation, by the quick transmission of high-temperature superconductor, do not changing on the basis of existing facility, Appropriate application superconducting characteristic also carries out the operating principle that humidity is extracted in cold-hot pressure contracting, utilizes humidification method to carry out functional combination, after adopting such system architecture, thus solve above high energy efficiency, the deficiency that air pollution is large.
Certainly, the potent air water intaking device of superconduction, also can be used on small air water intaking electrical equipment and in other structure, have multiple conversion and remodeling, be not limited in the concrete structure of above-mentioned embodiment, such conversion all drops within protection domain of the present utility model.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520172741.8U CN204849897U (en) | 2015-03-26 | 2015-03-26 | Superconductive strong effect water extraction from air machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520172741.8U CN204849897U (en) | 2015-03-26 | 2015-03-26 | Superconductive strong effect water extraction from air machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204849897U true CN204849897U (en) | 2015-12-09 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520172741.8U Expired - Fee Related CN204849897U (en) | 2015-03-26 | 2015-03-26 | Superconductive strong effect water extraction from air machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204849897U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105735416A (en) * | 2016-04-12 | 2016-07-06 | 顾美红 | A remote-controllable air-purifying water-making machine |
| CN109695268A (en) * | 2017-10-23 | 2019-04-30 | 李贺清 | A kind of method that fresh water is extracted on island |
-
2015
- 2015-03-26 CN CN201520172741.8U patent/CN204849897U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105735416A (en) * | 2016-04-12 | 2016-07-06 | 顾美红 | A remote-controllable air-purifying water-making machine |
| CN105735416B (en) * | 2016-04-12 | 2019-04-02 | 顾美红 | It is a kind of can remote control air cleaning water-making machine |
| CN109695268A (en) * | 2017-10-23 | 2019-04-30 | 李贺清 | A kind of method that fresh water is extracted on island |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151209 |