CN201648163U - Apparatus for desalination of sea water and purification of waste water by using natural energy - Google Patents
Apparatus for desalination of sea water and purification of waste water by using natural energy Download PDFInfo
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- CN201648163U CN201648163U CN2010201683830U CN201020168383U CN201648163U CN 201648163 U CN201648163 U CN 201648163U CN 2010201683830 U CN2010201683830 U CN 2010201683830U CN 201020168383 U CN201020168383 U CN 201020168383U CN 201648163 U CN201648163 U CN 201648163U
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- 239000013535 sea water Substances 0.000 title claims abstract description 62
- 238000010612 desalination reaction Methods 0.000 title claims abstract description 13
- 238000000746 purification Methods 0.000 title abstract description 15
- 239000002351 wastewater Substances 0.000 title abstract 3
- 238000001704 evaporation Methods 0.000 claims abstract description 80
- 230000008020 evaporation Effects 0.000 claims abstract description 80
- 239000007921 spray Substances 0.000 claims abstract description 71
- 238000009833 condensation Methods 0.000 claims abstract description 68
- 230000005494 condensation Effects 0.000 claims abstract description 68
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 51
- 238000010438 heat treatment Methods 0.000 claims abstract description 50
- 238000011282 treatment Methods 0.000 claims abstract description 29
- 238000001914 filtration Methods 0.000 claims abstract description 19
- 239000013505 freshwater Substances 0.000 claims abstract description 16
- 239000003921 oil Substances 0.000 claims description 105
- 239000011521 glass Substances 0.000 claims description 23
- 238000007747 plating Methods 0.000 claims description 20
- 238000000034 method Methods 0.000 claims description 18
- 239000000446 fuel Substances 0.000 claims description 17
- 238000005485 electric heating Methods 0.000 claims description 13
- 238000005507 spraying Methods 0.000 claims description 11
- 239000010724 circulating oil Substances 0.000 claims description 9
- 238000013022 venting Methods 0.000 claims description 8
- 230000002093 peripheral effect Effects 0.000 claims description 7
- 230000007704 transition Effects 0.000 claims description 7
- 239000010425 asbestos Substances 0.000 claims description 2
- 238000009434 installation Methods 0.000 claims description 2
- 238000009413 insulation Methods 0.000 claims description 2
- 229910052895 riebeckite Inorganic materials 0.000 claims description 2
- 238000009287 sand filtration Methods 0.000 claims description 2
- 238000012802 pre-warming Methods 0.000 abstract 3
- 239000010865 sewage Substances 0.000 description 51
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 7
- 229910052710 silicon Inorganic materials 0.000 description 7
- 239000010703 silicon Substances 0.000 description 7
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 5
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- 239000006227 byproduct Substances 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- FGRBYDKOBBBPOI-UHFFFAOYSA-N 10,10-dioxo-2-[4-(N-phenylanilino)phenyl]thioxanthen-9-one Chemical compound O=C1c2ccccc2S(=O)(=O)c2ccc(cc12)-c1ccc(cc1)N(c1ccccc1)c1ccccc1 FGRBYDKOBBBPOI-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
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- 230000009286 beneficial effect Effects 0.000 description 1
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- 230000007812 deficiency Effects 0.000 description 1
- 238000011033 desalting Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
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Images
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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
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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
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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
- Y02A20/142—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
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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
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
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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
- 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
-
- 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
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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
- 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
- Y02W10/33—Wastewater or sewage treatment systems using renewable energies using wind energy
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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
- 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
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- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model relates to an apparatus for desalination of sea water and purification of waste water by using natural energy. The utility model relates to an evaporation condense type water treatment system for desalination of sea water and purification of waste water by using natural energy of solar, wind energy and the like, wherein the system is composed of a filtering basin, a spray evaporation chamber, a vapor condensation device, a heat conduction oil heating pipe, a heat conduction oil heating device capable of employing the natural energy of the solar, the wind energy and the like, a solar battery set, a wind power generator, etc. the filtering basin is connected with a prewarming pool through a pipeline, the prewarming pool is connected with the spray evaporation chamber through a pressure pipeline, the spray evaporation chamber is connected with the vapor condensation device through a vapor pipeline, the lower end of the vapor condensation device is provided with a condensate water collection port communicated with a fresh-water pool through a pipeline, the back end of the vapor condensation device is provided with an exhaust outlet with an exhaust fan, the heat conduction oil heating pipe is arranged in the prewarming pool and the spray evaporation chamber and is connected with the heat conduction oil heating device through a heat conduction oil pipeline, and the solar battery set and the wind power generator provide energy for the heat conduction oil heating device.
Description
Affiliated technical field
The utility model relates to a kind of evaporative condenser formula water treatment device that can carry out sea water desaltination or sewage purification, the evaporative condenser formula water treatment device that especially can utilize natural energies such as the sun power of occurring in nature and wind energy just can carry out sea water desaltination, sewage purification.
Background technology
Now, a lot of cities, the whole world exist the resource-type lack of water of the problem, particularly some coastal coastal cities of fresh water shortage, solve the problem that these local water shortage problems can adopt the method solution lack of water of sea water desaltination or urban sewage purification.At present, known method for desalting seawater (freezing method, electroosmose process, distillation method, reverse osmosis) and sewage water treatment method (three grades of sewage treatments) all exist the fresh water that needs a large amount of corresponding energy of consumption and material just can obtain cleaning, the energy consumption of water treatment is big, and cost is higher.
Summary of the invention
For overcome present seawater, the sewage disposal energy consumption is big, the deficiency that cost is higher, the utility model provides the desalination of a kind of natural-energy seawater, effluent treatment plant, and this device utilizes natural energy such as the sun power, wind energy of occurring in nature just can carry out sea water desaltination or sewage purification.
Technical solution of the present utility model: the municipal effluent of seawater or the sewage disposal of process one-level intercepts transition bands after pipeline enters the preheating pond through three sections sandstone of filtering basin, the preheating pond is that a top is equipped with the certain space that has that is coated with the solar film plating coated glass that can absorb solar energy and can carries out pre-warmed semiclosed pond to a certain amount of seawater or sewage, heat-conducting oil heating pipe and pressure pump also are installed in the preheating pond, seawater or sewage are when entering the solar energy that the solar film plating coated glass that can absorb solar energy behind the preheating pond absorbs and being installed in that the common heating of pyritous thermal oil is issued to the optimal evaporation water temperature in the heat-conducting oil heating pipe in the pond, extract pressurization by the pressure pump in the preheating pond and enter the spray evaporation chamber through pressure pipeline, pressure type atomizer on spray evaporation room pressure pipeline or centrifugal spraying shower nozzle ejection atomizing, because of the spray evaporation chamber is to combine semi-enclosed have trapezoidal rectangular parallelepiped of certain space or semicylinder space by being coated with the solar film plating coated glass that can absorb solar energy, the spray evaporation chamber not only is equipped with the solar film plating coated glass that can absorb solar energy, the heat-conducting oil heating pipe also is installed, has very high room temp under the heating of spray evaporation chamber high temperature heat conductive oil in solar energy that the solar film plating coated glass absorbs and heat-conducting oil heating pipe, the atomizing seawater of atomizer ejection or sewage can be very fast under higher room temp on the spray evaporation intraventricular pressure solenoid flashes to water vapour (the water surrounding temperature of the atomizing effect of high evaporation more is just good more), salinity in seawater or the sewage or organic dirt will be deposited in spray evaporation indoor formation sodium-chlor sea salt or organic dirt, one side of evaporator room is provided with discharge port to be opened/closed, personnel can be to throw out cleaned at regular intervals discharging in the evaporator room, and the throw out that goes out clearly can be made into byproducts such as sodium-chlor sea salt or organic dirt fertilizer.Seawater after the evaporation or sewage water vapor enter vapour condensation device by the gathering of vertical vapor collection chamber, spray evaporation chamber through steam-pipe, vapour condensation device should be placed in the space in sunshade cool place, be to make by having the multistage combination of larger-diameter glass pipe or metallic conduit, the small-sized refrigerating condensing works can also be installed on the vapour condensation device water vapor in the vapour condensation device pipeline is carried out condensation liquefaction, vapour condensation device tail end venting port is equipped with exhaust fan makes the vapour condensation device pipeline be negative pressure exhaust to external world.Silicon single crystal that small-sized refrigerating condensing works and exhaust fan are settled through lead and peripheral hardware or polysilicon solar cell group and aerogenerator are electrically connected, by solar battery group and aerogenerator powered operation.The vapour condensation device lower end is provided with water of condensation collection mouth and is connected with fresh-water pool through pipeline.Entering the seawater of vapour condensation device or sewage water vapor becomes water of condensation and collects mouthful and connecting tube enters the sea water desaltination of evaporative condenser formula, the sewage purification water treatment procedure that fresh-water pool is finished seawater or sewage through water of condensation after vapour condensation device pipeline inner condensat liquidization.(for the water that is more cleaned, the water of condensation in the fresh-water pool can carry out the evaporative condenser formula water treatment procedure of secondary after through evaporative condenser formula water treatment procedure once again.) the preheating pond is connected with natural energy (sun power, wind energy) hot oil heater through thermal conductive oil pipeline with the indoor heat-conducting oil heating pipe of spray evaporation, the thermal oil recycle pump of pump separate type is installed on the thermal conductive oil pipeline, the natural energy hot oil heater is a kind of thermal oil fuel reserve tank of the N of being equipped with root solar energy vacuum tube, be marked with in the fuel reserve tank thermal oil through thermal conductive oil pipeline and preheating pond, the indoor heat-conducting oil heating pipe of spray evaporation is connected.Electric heating tube also is installed in the thermal oil fuel reserve tank, silicon single crystal that the thermal oil circulating pump motor of electric heating tube and pump separate type is settled through lead and peripheral hardware or monocrystaline silicon solar cell group and aerogenerator are electrically connected, by solar battery group and aerogenerator power supply.Thermal oil in the natural energy hot oil heater fuel reserve tank at solar energy that solar energy vacuum tube absorbs with by the electric heater for heating of solar battery group and aerogenerator power supply under thermal oil can reach 180 degrees centigrade high temperature, enter under the driving of the thermal oil circulating oil pump of pump separate type through thermal conductive oil pipeline and to give preheating pond maritime interior waters or sewage heating in the indoor heat-conducting oil heating pipe of preheating pond and spray evaporation, the space room temperature that is the spray evaporation chamber heats, and reaches to allow seawater or sewage desalinate at natural-energy seawater, carry out the sea water desaltination of evaporative condenser formula in the effluent treatment plant, the purpose of the water treatment of sewage purification.Natural energy hot oil heater fuel reserve tank and the corrosion resistant metal of heat-conducting oil pipes route are made, and cover on fuel reserve tank and the thermal conductive oil pipeline and are enclosed with the asbestos thermal insulation layer.
The beneficial effects of the utility model are just can carry out sea water desaltination or sewage purification at natural energies such as only utilizing sun power and wind energy.Have energy consumption little, do not consume other goods and materials, characteristics that cost of water treatment is low, can produce byproducts such as sodium-chlor sea salt or organic dirt fertilizer.The watt level of water treatment efficiency of the present utility model and natural energy hot oil heater is relevant with the condensation effect of vapour condensation device, and the high-power hot oil heater and the good vapour condensation device of condensation effect of many groups will improve the efficient of water treatment significantly.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1 is the utility model system construction drawing.
Fig. 2 is the utility model filtering basin structure iron.
Fig. 3 is the utility model preheating pool structure figure.
Fig. 4 is the utility model spray evaporation chamber first example structure sectional view.
Fig. 5 is the utility model spray evaporation chamber second example structure sectional view.
Fig. 6 is the utility model vapour condensation device and fresh-water pool section of structure.
Fig. 7 is the utility model natural energy hot oil heater structure and solar battery group and aerogenerator connection diagram.
1. pipelines among the figure, 2. filtering basin, 3. sandstone obstruct transition band, 4. preheating pond, 5. solar film plating coated glass, 6. heat-conducting oil heating pipe, 7. pressure pump, 8. pressure pipeline, 9. spray evaporation chamber, 10. pressure type atomizer or centrifugal spraying shower nozzle, vapor collection chambers 11., 12. vapour condensation devices, 13. small-sized refrigerating condensing works, 14. exhaust fan, the shady and cool space of 15. sunshades, 16. water of condensation are collected mouth, 17. venting port, 18. thermal conductive oil pipeline, 19. natural energy hot oil heaters, 20. solar energy vacuum tubes, 21. pump separate type thermal oil circulating oil pump, 22. electric heating tube, 23. circuit automatic control switch, 24. aerogenerators, 25. silicon single crystal or polysilicon solar cell group, 26. lead, 27. fresh-water pools, 28. discharge ports.
Embodiment
In Fig. 1, filtering basin 2 are connected with preheating pond 4 through pipeline 1, filtering basin 2 are one and have the sand filter method three-stage filtration pond that three sections sandstone intercept transition band 3, the city domestic sewage of seawater or the sewage disposal of process one-level enters filtering basin 2 by pipeline 1, intercepting transition band 3 through three grades of sandstone in the filtering basin filters after pipeline 1 enters preheating pond 4, preheating pond 4 is that a top is equipped with the certain space that has that is coated with solar film plating coated glass 5 that can absorb solar energy and can carries out pre-warmed semiclosed pond to a certain amount of seawater or sewage, heat-conducting oil heating pipe 6 and pressure pump 7 also are installed in the preheating pond 4, seawater or sewage back in flowing into preheating pond 4 can absorb the solar energy that the solar film plating coated glass 5 of solar energy absorbs and be installed under high temperature heat conductive oil in the heat-conducting oil heating pipe 6 in the preheating pond heats jointly, when reaching the optimal evaporation water temperature, extract pressurization by the pressure pump in the preheating pond 47, enter spray evaporation chamber 9 through pressure pipeline 8, pressure type atomizer on the pressure pipeline 8 in spray evaporation chamber 9 or the 10 ejection atomizings of centrifugal spraying shower nozzle.Because of spray evaporation chamber 9 is by being coated with the solar film plating coated glass 5 that can absorb solar energy semi-enclosed trapezoidal rectangular parallelepiped or the semicylinder space with certain space that is combined into to be installed, spray evaporation chamber 9 not only is equipped with the solar film plating coated glass 5 that can absorb solar energy heat-conducting oil heating pipe 6 also is installed, and spray evaporation chamber 9 has very high room temp under solar energy that solar film plating coated glass 5 absorbs and the high temperature heat conductive oil heat-conducting oil heating pipe 6 in heat.Seawater or sewage by 4 preheatings of preheating pond extract pressurization through pressure pump 7, in pressure pipeline 8 enters spray evaporation chamber 9, by pressure type atomizer on the pressure pipeline 8 or the 10 ejection atomizings of centrifugal spraying shower nozzle, the seawater of atomizing or sewage can be very fast under higher room temp flash to the water vapor (water after the atomizing, envrionment temperature is high more, the effect of evaporation is just good more), salinity in seawater or the sewage or dirt will be deposited in and form sodium-chlor sea salt or organic dirt in the spray evaporation chamber 9, one side of spray evaporation chamber 9 is provided with discharge port 28 to be opened/closed, personnel can carry out the cleaned at regular intervals discharging from 9 pairs of throw outs of discharge port 28 turnover evaporator rooms, the sodium-chlor sea salt or the organic dirt that go out clearly can become sea water desaltination, byproduct after the sewage purification, seawater or sewage water vapor in the spray evaporation chamber 9 are assembled in vertical vapor collection chambers 11 9, spray evaporation chamber, in steam-pipe enters vapour condensation device 12, vapour condensation device 12 is placed in the space 15 in sunshade cool place, be that larger-diameter glass pipe or metallic conduit are multistage to combine by having, the water vapor that can also be equipped with on the vapour condensation device 12 in 13 pairs of vapour condensation device 12 pipelines of small-sized refrigerating condensing works carries out condensation liquefaction, in the venting port 17 of vapour condensation device 12 tail ends exhaust fan 14 is installed, makes the vapour condensation device pipeline be negative pressure exhaust.Silicon single crystal that small-sized refrigerating condensing works 13 and exhaust fan 14 are settled through lead and peripheral hardware or polysilicon solar cell group 25 and aerogenerator 24 are electrically connected, by solar battery group 25 and aerogenerator 24 power supplies, vapour condensation device 12 lower end of duct are provided with water of condensation and collect mouth 16, entering fresh-water pool 27 by the pipeline that connects water of condensation collection mouth is connected, the water vapor that enters in vapour condensation device 12 pipelines becomes water of condensation after vapour condensation device pipeline inner condensat liquidization, collect mouthful 16 pipelines through water of condensation and enter fresh-water pool 27, finish the evaporative condenser formula sea water desaltination of seawater or sewage by connection water of condensation collection mouth, the sewage purification water treatment procedure.Preheating pond 4 is connected with natural energy hot oil heater 19 through thermal conductive oil pipeline 18 with spray evaporation chamber 9 interior heat-conducting oil heating pipes 6, the thermal oil circulating oil pump 21 of pump separate type is installed on the thermal conductive oil pipeline 18, natural energy hot oil heater 19 is thermal oil fuel reserve tanks of a kind of N of being equipped with root solar energy vacuum tube 20, is marked with thermal oil in the fuel reserve tank and is connected with heat-conducting oil heating pipe 6 in preheating pond 4, the spray evaporation chamber 9 through thermal conductive oil pipeline 18.In natural energy hot oil heater 19 fuel reserve tanks electric heating tube 22 is installed also, silicon single crystal that electric heating tube 22 and pump separate type thermal oil circulating oil pump 21 are settled through lead 26 and circuit automatic control switch 23 and peripheral hardware or polysilicon solar cell group 25 and aerogenerator 24 are electrically connected, under the control of circuit automatic control switch 23 by solar battery group 25 and aerogenerator 24 powered operations.Thermal oil in natural energy hot oil heater 19 fuel reserve tanks is under the solar energy and electric heating tube 22 heating by solar battery group 25 and aerogenerator 24 power supplies that solar energy vacuum tube 20 absorbs, thermal oil can reach 180 degrees centigrade high temperature, under the driving circulation of thermal conductive oil pipeline 18, enter the heat-conducting oil heating pipe 6 in preheating pond 4 and the spray evaporation chamber 9 at pump separate type thermal oil circulating oil pump 21, give seawater or sewage heating in the preheating pond 4, be the indoor space room temperature heat temperature raising of spray evaporation, reach and allow seawater or sewage desalinate at natural-energy seawater, carry out sea water desaltination in the effluent treatment plant system, the water treatment purpose of sewage purification.
In Fig. 2, filtering basin 2 are one and have the sand filtration method filtering basin that three grades of sandstone intercept transition band 3, the city domestic sewage of seawater or the sewage disposal of process one-level enters filtering basin 2 after three filtrations of sandstone obstruct transition band 3 through pipeline 1, enters preheating pond 4. through pipeline
In Fig. 3, preheating pond 4 is that a top is equipped with solar film plating coated glass 5, be equipped with in the pond heat-conducting oil heating pipe 6 and pressure pump 7 certain space arranged can carry out pre-warmed semiclosed pond to a certain amount of seawater or sewage, seawater or city domestic sewage are being filtered after pipeline enters in the preheating pond 4 by filtering basin 2, be issued to the optimal evaporation temperature at solar energy that absorbs by solar film plating coated glass 5 and the heating of the high temperature heat conductive oil in the heat-conducting oil heating pipe 6, extract pressurization in pressure pipeline 8 enters spray evaporation chamber 9 through force (forcing) pump 7, by pressure type atomizer on the pressure pipeline 8 or the 10 ejection atomizings of centrifugal spraying shower nozzle.
Fig. 4 is the first kind of embodiment in spray evaporation chamber, in Fig. 4, spray evaporation chamber 9 is trapezoidal rectangular parallelepiped hemi-closure spaces, 9 tops, spray evaporation chamber are equipped with solar film plating glass 5, heat-conducting oil heating pipe 6 is installed in the evaporator room, connect to advance on the pressure pipeline 8 in the spray evaporation chamber 9 by preheating pond 4 pressure type atomizer or centrifugal spraying shower nozzle 10 are installed, 9 tops, spray evaporation chamber are provided with vapor collection chamber 11, spray evaporation chamber one side is equipped with discharge port 28 to be opened/closed, and seawater or the sewage crossed via preheating pond 4 heating and pressurizing enter in the spray evaporation chamber 9 by pressure type atomizer on the pressure pipeline 8 or the 10 ejection atomizings of centrifugal spraying shower nozzle through pressure pipeline 8.Owing to have higher room temp under the heating of the space in the spray evaporation chamber 9 by the high temperature heat conductive oil in solar film plating coated glass solar energy that absorbs and the heat-conducting oil heating pipe 6 that is installed in the evaporator room, seawater after the atomizing or sewage is carburation by evaporation soon, vertical vapor collection chambers 9 11 gatherings enter vapour condensation device 12 through steam-pipe through the spray evaporation chamber, salinity in seawater or the sewage or dirt can precipitation separation in spray evaporation chamber 9, can be regular clean discharging by personnel from the discharge port 28 of spray evaporation chamber 9 one sides.
Fig. 5 is another kind of spray evaporation chamber embodiment, in the drawings, spray evaporation chamber 9 is hemi-closure spaces that are semicylinder, spray evaporation chamber 9 integral body are installed by the solar film plating coated glass and are combined, heat-conducting oil heating pipe 6 is installed in the spray evaporation chamber 9, connect to advance on the pressure pipeline 8 in the spray evaporation chamber 9 by preheating pond 4 pressure type atomizer or centrifugal spraying shower nozzle 10 are installed, 9 tops, spray evaporation chamber are provided with vapor collection chamber 11, spray evaporation chamber one side is equipped with discharge port 28 to be opened/closed, and seawater or the sewage crossed via preheating pond 4 heating and pressurizing enter in the spray evaporation chamber 9 by pressure type atomizer on the pressure pipeline 8 or the 10 ejection atomizings of centrifugal spraying shower nozzle through pressure pipeline 8.Owing to have higher room temp under the heating of the space in the spray evaporation chamber 9 by the high temperature heat conductive oil in solar film plating coated glass solar energy that absorbs and the heat-conducting oil heating pipe 6 that is installed in the evaporator room, seawater after the atomizing or sewage is carburation by evaporation soon, vertical vapor collection chambers 9 11 gatherings enter vapour condensation device 12 through steam-pipe through the spray evaporation chamber, salinity in seawater or the sewage or dirt can precipitation separation in spray evaporation chamber 9, can be regular clean discharging by personnel from the discharge port 28 of spray evaporation chamber 9 one sides.
Fig. 6 is vapour condensation device and fresh-water pool section of structure, vapour condensation device 12 is to combine by having the multistage installation of larger-diameter glass or metallic conduit among the figure, small-sized refrigerating condensing works 13 is installed on the vapour condensation device 12, in the vapour condensation device 12 tail end venting ports 17 exhaust fan 14 is installed, vapour condensation device 12 lower end of duct are provided with water of condensation and collect mouth 16 through pipe connection fresh-water pool 27, seawater or sewage water vapor are being assembled after steam-pipe enters in vapour condensation device 12 pipelines by the vapor collection chamber in the spray evaporation chamber 9 11, under effect, be vacuum flow to venting port 17 by the exhaust fan 14 in the vapour condensation device 12 tail end venting ports 17, when seawater or sewage water vapor flow in vapour condensation device 12 pipelines, because vapour condensation device is placed in the shady and cool space 15 of sunshade, under the condensation of small-sized refrigerating condensing works 13, has simultaneously lower temperature, seawater or sewage water vapor become water of condensation in vapour condensation device 12 pipeline inner condensat liquidizations, collect mouthful 16 gatherings by the water of condensation in the vapour condensation device and enter the evaporative condenser formula sea water desaltination that fresh-water pool 27 is finished seawater or sewage through pipeline, the sewage purification water treatment procedure.
In Fig. 7, natural energy hot oil heater 19 is the thermal oil fuel reserve tanks that N root solar energy vacuum tube 20 is installed, be marked with thermal oil in the fuel reserve tank, electric heating tube 22 also is installed, electric heating tube 22 is electrically connected through lead 26 and circuit automatic control switch 23 and silicon single crystal or polycrystalline silicon solar 25 and aerogenerator 24, heat-conducting oil heating pipe 6 in thermal conductive oil pipeline 18 connection preheating ponds 4 and the spray evaporation chamber 9 is arranged on natural energy hot oil heater 19 fuel reserve tanks, pump separate type thermal oil circulating oil pump 21 is installed on the thermal conductive oil pipeline 18, they have formed the natural energy heat-conducting oil heating recycle system jointly, thermal oil in natural energy hot oil heater 19 fuel reserve tanks is under solar energy that is absorbed by solar energy vacuum tube 20 and the heating by the electric heating tube 22 of solar battery group 25 and aerogenerator 24 power supplies, reach as high as 180 degrees centigrade high temperature, the pyritous thermal oil under by the driving of pump separate type thermal oil circulating oil pump 21 through thermal conductive oil pipeline 18 at whole natural energy hot oil heater system internal recycle, give seawater or sewage heating in the preheating pond 4, be the room temps heating of spray evaporation chamber 9, cooperate whole natural-energy seawater desalination, effluent treatment plant is finished the water treatment procedure of sea water desaltination or sewage purification.
Claims (6)
1. natural-energy seawater desalination, effluent treatment plant, by filtering basin, the preheating pond, the spray evaporation chamber, vapour condensation device and fresh-water pool are through the pipe connection intercommunication, with the heat-conducting oil heating pipe, the common a kind of natural-energy seawater desalination formed of natural energy hot oil heater and solar battery group and aerogenerator, effluent treatment plant, it is characterized in that: filtering basin are connected with the preheating pond through pipeline, top, preheating pond is equipped with the solar film plating coated glass, heat-conducting oil heating pipe and pressure pump are installed in the pond, through the pressure pipeline intercommunication that is connected with the spray evaporation chamber, on the indoor pressure pipeline of spray evaporation atomizer is installed, the indoor heat-conducting oil heating pipe that is equipped with, spray evaporation chamber one side is provided with discharge port to be opened/closed, top, spray evaporation chamber is provided with the vapor collection chamber and is connected with vapour condensation device through steam-pipe, vapour condensation device is equipped with the small-sized refrigerating condensing works, the vapour condensation device lower end is provided with water of condensation collection mouth and is connected with fresh-water pool through pipeline, the vapour condensation device tail end is the venting port that exhaust fan is installed, the preheating pond is connected with the natural energy hot oil heater through thermal conductive oil pipeline with the heat-conducting oil heating pipe of the indoor installation of spray evaporation, the thermal oil circulating oil pump of pump separate type is installed on the thermal conductive oil pipeline, be marked with thermal oil in the natural energy hot oil heater and electric heating tube is installed, electric heating tube is through the solar battery group of lead and peripheral hardware arrangement, aerogenerator is electrically connected.
2. natural-energy seawater desalination according to claim 1, effluent treatment plant is characterized in that: filtering basin are a kind of three grades of sand filtration method filtering basin that three sections sandstone intercept transition band that are provided with.
3. natural-energy seawater desalination according to claim 1, effluent treatment plant, it is characterized in that: the preheating pond is the semiclosed pond that a kind of top is equipped with the solar film plating coated glass, and heat-conducting oil heating pipe and pressure pump also are installed in the preheating pond.
4. natural-energy seawater desalination according to claim 1, effluent treatment plant, it is characterized in that: the spray evaporation chamber is by being coated with the solar film plating coated glass semi-enclosed trapezoidal rectangular parallelepiped or the semicylinder space combine to be installed, pressure type atomizer or centrifugal spraying shower nozzle are installed on the pressure pipeline that spray evaporation is indoor with the preheating pond communicates, the centrifugal spraying shower nozzle is a kind of rotary and centrifugal type atomizer that has centrifugal flywheel and micromotor, the indoor heat-conducting oil heating pipe that also is equipped with of spray evaporation, the top is provided with the vapor collection chamber, and spray evaporation chamber one side is provided with discharge port to be opened/closed.
5. natural-energy seawater desalination according to claim 1, effluent treatment plant, it is characterized in that: vapour condensation device is equipped with the small-sized refrigerating condensing works, the vapour condensation device lower end is provided with water of condensation collection mouth and is connected with fresh-water pool through pipeline, the vapour condensation device tail end is the venting port that exhaust fan is installed, vapour condensation device is placed in the shady and cool space of sunshade, and small-sized refrigerating condensing works and exhaust fan are electrically connected through the solar battery group and the aerogenerator of lead and peripheral hardware arrangement.
6. natural-energy seawater desalination according to claim 1, effluent treatment plant, it is characterized in that: the natural energy hot oil heater is a kind of thermal oil fuel reserve tank of the N of being equipped with root solar energy vacuum tube, be marked with thermal oil in the fuel reserve tank and electric heating tube is installed, electric heating tube is through the solar battery group of lead and peripheral hardware arrangement, aerogenerator is electrically connected, the thermal oil circulating oil pump of pump separate type is installed on the thermal conductive oil pipeline, with be installed in the preheating pond, the common connection of heat-conducting oil heating pipe that spray evaporation is indoor and thermal conductive oil pipeline is combined into the natural energy heat-conducting oil heating recycle system, and the fuel reserve tank of natural energy hot oil heater and thermal conductive oil pipeline cover and be enclosed with the asbestos thermal insulation layer.
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