CN201495111U - Solar multifunctional seawater desalting system - Google Patents
Solar multifunctional seawater desalting system Download PDFInfo
- Publication number
- CN201495111U CN201495111U CN2009201487832U CN200920148783U CN201495111U CN 201495111 U CN201495111 U CN 201495111U CN 2009201487832 U CN2009201487832 U CN 2009201487832U CN 200920148783 U CN200920148783 U CN 200920148783U CN 201495111 U CN201495111 U CN 201495111U
- Authority
- CN
- China
- Prior art keywords
- unit
- water
- low
- vacuum type
- water tank
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
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
-
- 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
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model discloses a solar multifunctional seawater desalting system, comprising a water supply unit, a solar casing management system unit, a condensed water tank unit, an intelligent plastic porous guiding valve unit, a low-temperature evaporated gas collecting and condenser unit, and a concentrated solution collector unit which are disposed independently. The water supply unit is orderly connected with the solar casing management system unit and the condensed water tank unit. Two rows of passages are disposed on the solar casing management system unit, wherein one row is orderly connected with the intelligent plastic porous guiding valve unit and the low-temperature evaporated gas collecting and condenser unit and other row is orderly connected with the concentrated solution collector unit. The utility model has low running cost, low investment cost, and easy management. The solar multifunctional seawater desalting system can simultaneously desalt seawater, sewage, salty bitter water, ice and snow, river water, well water, and the like, and can be applied to recycling and absorbing heat energy, cooling and warming, and the like.
Description
Technical field
The utility model relates to a kind of seawater desalination system, refers to a kind of solar energy multifunctional seawater desalination system especially, and it is used for sea water desaltination, sewage purification, drinking water treatment or extracts various elements etc. from water, and has function such as cooling and warming concurrently.
Background technology
Recently the contaminated degree of seawater is serious all the more, particularly its bacterium, organic compound, mineral oils, county's floating particles thing etc. have influenced the seawater hygienic quality in the seawater on greater coasting area and top layer, be unfavorable for that the mankind get its desalination and drink, hindered the normal growth of famous and precious fishes and shrimps to grow, and desalinating cost increases in desalting process, and the dope discharging has caused the environmental pollution in land and coastal waters.
And deep sea water is nutritious and lack contaminated, deep sea water is meant off sea seawater below 200 meters of benthos, the depths, sea is difficult to see sunlight, the few bacterium of low temperature, thereby the organism decomposition rate exceeds resultant velocity greatly, in the process that organism promptly decomposes in a large number, produced abundant nitrogenous, phosphorous nutrition, take or desalinate the bathypelagic salt water supply mankind and be used as heath food, and production novel food product, bring up famous and precious fishes and shrimps, wake up and put cosmetics etc., all have great economic benefit and development prospect.
Existingly extract the technology that the shallow sea seawater is desalinated on land, the one, extract contaminated coastal waters surface water, contained suspended substance, silt, pollution compound are more, need a large amount of pre-processing device of investment, and having taken a large amount of soils, the operating period also need be dropped into manpower, medicine, electric power etc.; The 2nd, in desalting process, need pressurization to separate, desalination water rate only 30%～50%, the dynamic power that is consumed is bigger; The 3rd, the condensed water of palpus discharging 50%～70% has not only been wasted handling charges, electricity expense usefulness, pre-treatment expense etc., and has been polluted environment in the desalination process, comprises that inshore environment all has been subjected to pollution.
Except above-mentioned seawater contaminated serious, the many water resourcess in the society also have been subjected to pollution now, as river or lake water, and tap water and so on, and society's utilization of advocating thriftiness water, improving reuse water at present, to satisfy the social demand of lack of water.Therefore, the technology of sewage disposal, desalting plant that is used for sea water desaltination, sewage purification, drinking water treatment or extracts functions such as various elements from water is also accordingly in continuous improve.
The utility model content
In view of the water desalination techniques of above-mentioned existence wait improve, order of the present utility model is for a kind of problem that can better solve lack of water is provided, can desalinate the solar energy multifunctional seawater desalination system of handling seawater, sewage, salty misery, ice and snow, river, well water etc. simultaneously, and have energy recovery, absorption, function such as freeze, heat.
To achieve these goals, technical solution of the present utility model is:
A kind of solar energy multifunctional seawater desalination system, be provided with the waterworks unit, sun power cannula system unit, the condensation water tank unit, guide valve unit, intelligence plasticity multitube hole, low-temperature evaporation collection and confinement of gases and condenser unit, the concentrated solution collector unit, described waterworks unit, sun power cannula system unit, the condensation water tank unit, guide valve unit, intelligence plasticity multitube hole, low-temperature evaporation collection and confinement of gases and condenser unit, the concentrated solution collector unit independently is provided with, the waterworks sequence of unit connects sun power cannula system unit and condensation water tank unit, sun power cannula system unit is provided with two row's passages, wherein one arrange and guide valve unit, intelligent plasticity multitube hole, low-temperature evaporation collection and confinement of gases and condenser unit are linked in sequence, and another row is connected with concentrated solution withdrawer sequence of unit.
Be provided with water pretreatment pool unit, pumping device unit in the described waterworks unit, add the water tank unit automatically, all be linked in sequence.
Be provided with vacuum type endothermic tube system element, water vapo(u)rization system unit in the described sun power cannula system unit, all be linked in sequence.
Described vacuum type endothermic tube system element is provided with the above vacuum type endothermic tube unit of one-level at least.
After adopting such scheme, the utility model adopts the solar energy multifunctional seawater desalination system, be provided with waterworks unit, sun power cannula system unit, condensation water tank unit, guide valve unit, intelligent plasticity multitube hole, low-temperature evaporation collection and confinement of gases and condenser unit, concentrated solution collector unit, can not need operation power, drive mobile material by solar-powered thermal.Advantages such as its running cost is low, and cost of investment is low, and is manageable.No matter be in remote mountain area, island, desert, ship's and crafts, severe winter the area, or be in the city, small towns etc. Anywhere, as long as there is the place of the sun and seawater (or other any water quality) can utilize the utility model to obtain high-quality fresh water.Or else need the consumptive material operation behind the utility model one-time investment, both can from seawater (or other any water quality), obtain cleaning water, can before seawater (or other any water quality) evaporation, extract material, reclaim again, perhaps after water is evaporated, extract, reclaim various mineral salts, miniature organism body, heavy metal, rare elements, trace element and other useful material again prior to the water evaporation.Be applied in energy recovery, absorption, there is better practicality aspect such as freeze, heat.
The utility model is described in further detail below in conjunction with drawings and embodiments:
Description of drawings
Fig. 1 is the light system chart of the utility model solar energy multifunctional seawaterization;
Fig. 2 is the utility model waterworks unit block diagram;
Fig. 3 is the utility model sun power cannula system unit block diagram;
Fig. 4 is the utility model vacuum type endothermic tube system element block diagram;
Fig. 5 is the utility model vacuum type endothermic tube unit block diagram;
Fig. 6 is the utility model water vapo(u)rization system unit block diagram;
Fig. 7 is the utility model vacuum type water generating tube unit block diagram;
Fig. 8 is the utility model condensation water tank unit block diagram;
Fig. 9 is the utility model low-temperature evaporation collection and confinement of gases, condenser unit block diagram.
The figure number explanation:
1 waterworks unit, 10 water pretreatment pool units
11 pumping device unit 12 add the water tank unit automatically
2 sun power cannula system unit, 20 vacuum type endothermic tube system elements
2000 1# level vacuum type endothermic tube unit, 200 vacuum type endothermic tube unit
2002 3# level vacuum type endothermic tube unit, 2001 2# level vacuum type endothermic tube unit
2003 last n-2# level vacuum type endothermic tube unit
2004 last n-1# level vacuum type endothermic tube unit
2005 last n# level vacuum type endothermic tube unit
The built-in feed liquor thrust-augmenting nozzle of 20000 endothermic tubes
210 vacuum type water generating tube unit, 21 water vapo(u)rization system unit
2100 1# level vacuum type water generating tube unit
2101 2# level vacuum type water generating tube unit
2102 last n-1# level vacuum type water generating tube unit
2103 last n# level vacuum type water generating tube unit
The built-in feed liquor thrust-augmenting nozzle of 21000 generating tubes
3 condensation water tank unit
30 water vapor collector unit, 31 prolong unit
32 condensate collector unit
Guide valve unit, 4 intelligent plasticity multitube hole
5 low-temperature evaporation collection and confinement of gases, condenser unit
50 low-temperature evaporation gas trap unit, 51 condenser units
6 concentrated solution collector unit
Embodiment
The solar energy multifunctional seawater desalination system, it is provided with waterworks unit 1, sun power cannula system unit 2, condensation water tank unit 3, guide valve unit, intelligent plasticity multitube hole 4, low-temperature evaporation collection and confinement of gases and condenser unit 5, concentrated solution collector unit 6, described waterworks unit 1, sun power cannula system unit 2, condensation water tank unit 3, guide valve unit, intelligent plasticity multitube hole 4, low-temperature evaporation collection and confinement of gases and condenser unit 5, concentrated solution collector unit 6 independent settings, as shown in Figure 1.Guide valve unit, described intelligent plasticity multitube hole 4, by different temperature, humidity and pressure, control stretching, contracting of different gels, allow the gel intellectuality, need not to control the circulation of pipeline flexibly under the automatically controlled condition, substituting the function of machinery valve, omit greatly automatically controlled, the automatically investment and the management of control, monitoring equipment.Described waterworks unit 1 be linked in sequence sun power cannula system unit 2 and condensation water tank unit 3, sun power cannula system unit 2 also are provided with two row's passages in addition: one of them row is linked in sequence with guide valve unit, intelligent plasticity multitube hole 4, low-temperature evaporation collection and confinement of gases and condenser unit 5; Two rows wherein are linked in sequence with concentrated solution collector unit 6.
As shown in Figure 2, be provided with water pretreatment pool unit 10, pumping device unit 11 in the waterworks unit 1, add water tank unit 12 automatically, all be linked in sequence.Wherein, described waterworks unit 1 can be provided with the water pretreatment pool unit, sets according to different water quality, and the utility model omits; Pumping device unit 11 can be manual, electronic, solar boosted or adopt other water pumping power.
As shown in Figure 3, be provided with vacuum type endothermic tube system element 20, water vapo(u)rization system unit 21 in the sun power cannula system unit 2, all be linked in sequence.Cooperate shown in Figure 4, after water (after waterworks unit 1 initial purge) enters vacuum type endothermic tube unit 200, just begin to carry out steppedly to heat up in proper order from 1# level vacuum type endothermic tube unit 2000, order is by other vacuum type endothermic tubes at different levels, to the last behind the n# level vacuum type endothermic tube unit 2005, enter the vacuum type water generating tube unit 210 of water vapo(u)rization system unit 21 again through guide valve unit, intelligent plasticity multitube hole 4 orders.
Described vacuum type endothermic tube system element 20 is made up of numerous vacuum type endothermic tubes unit 200, the quantity of vacuum type endothermic tube unit 200 designs as required and increases, subtracts, every grade of vacuum type endothermic tube unit is equipped with independently steam flow-guiding mouth and liquid inlet and outlet (the steam flow-guiding mouth is connected single with intelligent plasticity multitube hole guide valve, low-temperature evaporation collection and confinement of gases, condenser unit are all single in proper order, and liquid inlet and outlet is the mutually tight Link Port of order between the vacuum type endothermic tube unit).
As shown in Figure 5, be provided with the built-in feed liquor thrust-augmenting nozzle 20000 of endothermic tube in the vacuum type endothermic tubes at different levels unit 2000～2005 of vacuum type endothermic tube unit 200.
As shown in Figure 6, the water after the intensification enters after the vacuum type water generating tube unit 210, and the generation water vapor that vacuum type water generating tube unit at different levels (2100～2103) just can be very fast, water vapor generate the water vapor collector unit 30 that the back order enters condensation water tank unit 3.Cooperate shown in Figure 7ly, be provided with the built-in feed liquor thrust-augmenting nozzle 21000 of generating tube in the vacuum type water generating tube unit 2100～2103 of vacuum type water generating tube unit 210.As shown in Figure 8, water vapor enters behind the water vapor collector unit 30 of condensation water tank unit 3 just order and enters prolong unit 31 and carry out condensation, is pure fresh water after the water vapor that is condensed becomes water and enters condensate collector unit 32.
As shown in Figure 9,50 orders enter condenser unit 51 to the residual solution that is concentrated at last from low-temperature evaporation gas trap unit.
The utility model is to utilize the solar energy direct irradiation on sun power cannula system unit 2, drive mobile material (seawater or any other water quality) by solar-powered thermal, in the vacuum type endothermic tube unit 200 of different temperature, flow, evaporation, prior to the material of water evaporation along with the lifting of temperature is condensed immediately and collects by progressive evaporation in advance and through low-temperature evaporation collection and confinement of gases, condenser unit 5.When temperature reaches the temperature of water evaporation, just be evaporated in the seawater of sun power cannula system unit 2 or other any water quality and be water vapor, water vapor is condensed just can obtain clean water.Simultaneously, the residual substance that the end is evaporated (as: mineral salt, life elements etc.) concentrates through sun power, and becoming is more prone to be extracted, and some rare elements become after by of the present utility model concentrating more the economic worth of recovery, extraction.
In sum, after the utility model adopts above-mentioned setting and flow process, can well solve: the domestic water of water-deficient area; Various sewage disposals; Various nuisance qualitative changes are given up precious in the recycle-water; Extract a comprehensive difficult problem such as various Mineral resources, biological residual body or trace element in the water.Be applied in energy recovery, absorption, functions such as cooling and warming have better practicality, and energy-saving effect is desirable more.
Above embodiment is only for the usefulness that the utility model is described, but not to restriction of the present utility model, person skilled in the relevant technique under the situation that does not break away from spirit and scope of the present utility model, can also be made various conversion or variation.Therefore, all technical schemes that are equal to also should belong to category of the present utility model, should be limited by each claim.
Claims (4)
1. solar energy multifunctional seawater desalination system, it is characterized in that: be provided with the waterworks unit, sun power cannula system unit, the condensation water tank unit, guide valve unit, intelligence plasticity multitube hole, low-temperature evaporation collection and confinement of gases and condenser unit, the concentrated solution collector unit, described waterworks unit, sun power cannula system unit, the condensation water tank unit, guide valve unit, intelligence plasticity multitube hole, low-temperature evaporation collection and confinement of gases and condenser unit, the concentrated solution collector unit independently is provided with, the waterworks sequence of unit connects sun power cannula system unit and condensation water tank unit, sun power cannula system unit is provided with two row's passages, wherein one arrange and guide valve unit, intelligent plasticity multitube hole, low-temperature evaporation collection and confinement of gases and condenser unit are linked in sequence, and another row is connected with concentrated solution withdrawer sequence of unit.
2. solar energy multifunctional seawater desalination system as claimed in claim 1 is characterized in that: be provided with water pretreatment pool unit, pumping device unit in the described waterworks unit, add the water tank unit automatically, all be linked in sequence.
3. solar energy multifunctional seawater desalination system as claimed in claim 1 is characterized in that: be provided with vacuum type endothermic tube system element, water vapo(u)rization system unit in the described sun power cannula system unit, all be linked in sequence.
4. solar energy multifunctional seawater desalination system as claimed in claim 3 is characterized in that: described vacuum type endothermic tube system element is provided with the above vacuum type endothermic tube unit of one-level at least.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201487832U CN201495111U (en) | 2009-03-30 | 2009-03-30 | Solar multifunctional seawater desalting system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201487832U CN201495111U (en) | 2009-03-30 | 2009-03-30 | Solar multifunctional seawater desalting system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201495111U true CN201495111U (en) | 2010-06-02 |
Family
ID=42438319
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009201487832U Expired - Fee Related CN201495111U (en) | 2009-03-30 | 2009-03-30 | Solar multifunctional seawater desalting system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201495111U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111233235A (en) * | 2020-01-16 | 2020-06-05 | 广东省实验动物监测所 | Ultrapure water instrument system |
-
2009
- 2009-03-30 CN CN2009201487832U patent/CN201495111U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111233235A (en) * | 2020-01-16 | 2020-06-05 | 广东省实验动物监测所 | Ultrapure water instrument system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP6154023B2 (en) | Seawater desalination apparatus and method using solar energy continuous heat supply | |
| CN104671313B (en) | Solar sea water desalination device | |
| CN103663589B (en) | Seawater desalinization method and seawater desalinization device | |
| CN212504424U (en) | Landscape seawater desalination platform for leisure/rescue | |
| CN102826700A (en) | Solar membrane distillation seawater desalination plant for sea island | |
| CN101880069A (en) | Negative pressure strengthened multi-stage laminated disc type solar energy distillation system for desalination | |
| CN101838024A (en) | Driven flash-evaporation solar seawater desalination method and device | |
| CN204643892U (en) | A kind of solar energy sea water desalination apparatus | |
| CN203820489U (en) | Low-temperature evaporation treatment device for high-concentration wastewater | |
| CN210150894U (en) | Efficient energy-saving zero-emission treatment device | |
| CN2619929Y (en) | Solar device for seawater desalination | |
| CN201495111U (en) | Solar multifunctional seawater desalting system | |
| CN201864592U (en) | Full-automatic solar seawater desalination device | |
| CN103232083B (en) | A kind of solar wind-energy Low pressure seawater desalination plant | |
| CN105753084A (en) | Photo-thermal seawater distillation and desalination device | |
| CN203006975U (en) | Solar continuous heat supply seawater desalination device | |
| CN212712829U (en) | Solar photo-thermal seawater desalination integrated system | |
| CN203959979U (en) | A kind ofly utilize the solar powered energy-conservation water system of making | |
| CN203790602U (en) | Alcohol atmospheric distillation and waste-liquid concentration thermal coupling system of molasses materials | |
| CN215906032U (en) | Seawater desalination device with solar heating film | |
| CN220131932U (en) | Solar sea water desalination and refined salt refining device | |
| CN221296252U (en) | Concentrated mine water/high-salinity wastewater desalting device for low flow and high salinity | |
| CN221254016U (en) | Device for desalting brine and alkaline water by solar energy | |
| CN202924779U (en) | Solar brackish water and seawater desalination device | |
| CN208279338U (en) | Solar energy total heat recovery self-operating efficient sea water desalting equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100602 Termination date: 20120330 |