CN210885391U - Small split solar electrostatic atomization seawater desalination device - Google Patents
Small split solar electrostatic atomization seawater desalination device Download PDFInfo
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- CN210885391U CN210885391U CN201920884529.2U CN201920884529U CN210885391U CN 210885391 U CN210885391 U CN 210885391U CN 201920884529 U CN201920884529 U CN 201920884529U CN 210885391 U CN210885391 U CN 210885391U
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- seawater
- electrostatic atomization
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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
- Y02A20/142—Solar thermal; Photovoltaics
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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
- Y02A20/20—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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Abstract
The utility model relates to a small-size split type solar energy electrostatic atomization sea water desalination device improves solar energy sea water desalination device evaporation efficiency through electrostatic atomization technique. The device mainly comprises a condensation chamber, a heat exchange tube, an evaporation chamber, an electrostatic atomization device, a seawater water storage tank, a control box and a solar heat collection tube. The electrostatic atomization device atomizes seawater into micron-sized fine particles, the micron-sized fine particles are adsorbed to the surface of the heat exchange tube under the action of a high-voltage electrostatic field, and after the particle size of liquid drops is reduced, the surface contact area of unit volume of seawater is rapidly increased, namely the heating area of the seawater is increased. The solar heat collecting tube absorbs heat energy of sunlight to heat the heat exchange medium in the heat collecting tube, after the heat exchange medium reaches a set temperature, the control box controls the water pump to enable the heated heat exchange medium to circulate between the heat exchange tube and the solar heat collecting tube, the temperature of the heat exchange tube is increased, and seawater atomized particles adsorbed on the heat exchange tube are heated and evaporated; after the seawater is evaporated on the surface of the heat exchange tube, water vapor is generated and condensed into fresh water in the condensation chamber.
Description
Technical Field
The utility model belongs to the technical field of the sea water desalination and specifically relates to a small-size split type solar energy electrostatic atomization sea water desalination device.
Background
The current mainstream solar seawater desalination method can be divided into a passive type method and an active type method, wherein the passive type device has the advantages of simple structure, convenient material taking, low energy consumption and low water yield per unit area; most active devices are matched with methods such as multi-stage flash evaporation, low temperature and multiple effects, and the like, and need to be matched with auxiliary facilities, so that the whole set of device is high in manufacturing cost, high in maintenance difficulty and capable of consuming certain energy, and is suitable for large and medium-sized seawater desalination devices.
For example, the invention patent with publication number CN105540709A discloses a seawater desalination device, which comprises a heater, a heating water pipeline and an evaporation chamber, wherein a heating pipe is arranged in the heater, the heater is connected with the heating water pipeline, the heating water pipeline enters from one side of the lower part of the evaporation chamber and penetrates out from the other side of the lower part of the evaporation chamber, the bottom of the evaporation chamber is also connected with a seawater inlet pipeline and a seawater outlet pipeline, the lower part of the evaporation chamber is filled with seawater entering the evaporation chamber from the seawater inlet pipeline, the upper part of the evaporation chamber is steam generated by heating seawater by hot water in the heating water pipeline, a condenser is arranged at the upper part of the evaporation chamber, a connected fresh water tank is arranged below the condenser, the fresh water tank is connected with a fresh water pipeline and a water suction pump, the fresh water pipeline penetrates out from one side; the device comprises an evaporation chamber, a compressor, a siphon pipe, a heating water pipeline and a heater, wherein the evaporation chamber is arranged at the top of the evaporation chamber, one end of the steam pipeline is communicated with the top of the evaporation chamber, the other downward end of the steam pipeline is communicated to the bottom of the evaporation chamber, the compressor is arranged on the steam pipeline to recover steam which is not completely condensed, the siphon pipe is also connected to the outer side of the evaporation chamber, one end of the siphon pipe is communicated to the inside of the evaporation chamber, the end face of the siphon pipe is positioned on the surface. The whole supporting facility of this sea water desalination device is many and cost is with high costs, the maintenance degree of difficulty is great, and this patent purpose mainly reduces sea water desalination device cost, towards the security, and the miniaturization, lightweight improves.
SUMMERY OF THE UTILITY MODEL
The utility model aims at solving the defects in the prior art and providing a small-sized split solar electrostatic atomization seawater desalination device.
In order to realize the purpose, the utility model discloses a technical scheme as follows:
a small split type solar electrostatic atomization seawater desalination device comprises a solar heat collecting pipe, a seawater water storage tank, an electrostatic atomization device, an evaporation chamber, a heat exchange pipe and a condensation chamber, wherein the heat exchange pipe is assembled in the evaporation chamber;
a medium water pump is arranged between the heat exchange tube and the solar heat collection tube, a water inlet of the medium water pump is connected with the solar heat collection tube, a water outlet of the medium water pump is connected with a water inlet of the heat exchange tube, a water outlet of the heat exchange tube is connected back to the solar heat collection tube through a water pipe, and a heat exchange medium circulates between the heat exchange tube and the solar heat collection tube through the.
Further, the electrostatic atomization device comprises a spray needle, a spray needle support, an installation base, a base support and a water inlet pipe; the spray needle is connected with the water inlet pipe through a tee joint quick connector, the head of the spray needle extends into the evaporation chamber, the quick connector is embedded into a groove of the spray needle support for fixation, the spray needle support is fixed on the mounting base through threads, and the base support is placed below the mounting base; the area supported by the base is smaller than that of the mounting base.
Furthermore, the pipelines of the water inlet pipe are kept on the same plane, and four spray needles of the electrostatic atomization device are arranged in a symmetrical structure by taking the water inlet pipe as the center. The flow velocity of each spray needle is kept consistent, and the seawater particles atomized by the four spray needles are uniformly adsorbed on the heat exchange tube.
The seawater desalting device further comprises a control box, wherein the control box is placed on the side face of the evaporation chamber and locked with the side face of the evaporation chamber through threads, the control box comprises a high-pressure generator, a seawater pump, a medium pump, a sensor and a central controller, and the positive end and the negative end of the high-pressure generator are respectively connected with the spray needle and the heat exchange tube through leads; the sensor is attached to the surface of the heat exchange tube to collect the temperature of the heat exchange tube in real time, the central controller is communicated with the sensor through a serial port, the seawater pump is connected with the seawater water storage tank and the water inlet tube of the electrostatic atomization device through a guide tube, and the medium water pump is connected with the solar heat collection tube and the heat exchange tube through a guide tube.
Furthermore, the heat exchange tube is positioned in the center of the evaporation chamber, the distance between two side surfaces of the heat exchange tube and the nearest inner wall of the evaporation chamber is 5 cm, and the four spray needles are respectively positioned in the middle areas between the two side surfaces of the heat exchange tube and the inner wall of the evaporation chamber; the heat exchange tube is placed right above the mounting base of the electrostatic atomization device, the vertical distance between the top ends of the spray needles and the heat exchange tube is 5 cm, and meanwhile, the four spray needles are inwardly deviated by 5 degrees. When the electrostatic atomization device works, seawater atomized liquid drops are filled between the heat exchange tube and the four walls of the evaporation chamber.
Furthermore, the condensing chamber comprises a condensing chamber main body and a condensing chamber top cover, four edges in the condensing chamber main body are provided with fresh water collecting tanks, the fresh water collecting tanks are connected with fresh water collecting pipes, and the fresh water collecting pipes are flush with the lower surface of the condensing chamber main body; the water vapor is condensed into required fresh water on the top cover of the condensing chamber and the inner wall of the condensing chamber main body and stored in the fresh water collecting tank;
the top of condensing chamber top cap has trickle pipe, catch basin piece, honeycomb duct, and catch basin piece perpendicular to condensing chamber top cap is placed, through the sea water pump of control box supplies water for the trickle pipe, and it has the aperture to open on the trickle pipe, and the sea water through the trickle pipe can flow into the catch basin piece through the aperture, and the honeycomb duct is connected to the catch basin piece.
Furthermore, the top cover of the condensing chamber forms an included angle of 15-30 degrees with the horizontal plane. The condensing area is increased, and meanwhile, the water condensed on the top cover of the condensing chamber slides into the fresh water collecting tank along the inclined surface.
Furthermore, the diversion pipe is connected with the seawater storage tank through a guide pipe, and the diversion pipe exchanges heat with seawater in the seawater storage tank. Seawater flowing through the top cover of the condensing chamber can absorb heat while condensing fresh water in an accelerating manner, and then flows back to the seawater water storage tank through the diversion pipe.
The utility model has the advantages that: 1. the heat collecting pipe, the electrostatic atomization device, the seawater water storage tank, the heat exchange pipe and the condensation chamber adopt a split structure, work independently and have good replaceability.
2. The electrostatic atomization device adopts a two-layer structure, the base supporting area is small, the electrostatic atomization device is arranged below the installation base, a passage for seawater to contact with the seawater water storage tank through the base supporting and installation base is cut off, and the effect of safe insulation is achieved.
3. The seawater used for condensation on the top cover of the condensation chamber is heated and then flows back to the seawater water storage tank, and the seawater which is not evaporated on the heat exchange tube can also flow back to the seawater water storage tank, so that the heat energy can be more fully utilized.
4. The heat exchange tube is positioned in the center of the evaporation chamber, the four spray needles are distributed on two side surfaces of the heat exchange tube, when the electrostatic atomization device works, seawater atomization liquid drops are filled between the heat exchange tube and the four walls of the evaporation chamber, and the heat of the heat exchange tube can act on the atomized seawater liquid drops for a more sufficient time and cannot be dissipated through the outer wall of the evaporation chamber.
5. The control box, the seawater water storage tank, the evaporation chamber, the heat exchange tube and the condensation chamber are all grounded, so that the device shell is prevented from generating high voltage, and potential safety hazards are avoided.
Drawings
FIG. 1 is a schematic structural diagram of a solar seawater desalination plant of the present apparatus;
FIG. 2 is a schematic structural view of an electrostatic atomizer according to the present invention;
FIG. 3 is a schematic structural diagram of a condensing chamber of the device;
fig. 4 is a schematic view of the internal structure of the control box of the device.
Detailed Description
Referring to fig. 1, a small split solar electrostatic atomization seawater desalination device mainly comprises a condensation chamber 1, a heat exchange tube 2, an evaporation chamber 3, an electrostatic atomization device 4, a seawater water storage tank 5, a control box 6 and a solar heat collection tube 7. The bottom of the solar heat collecting tube 7 is provided with a reflecting sheet, the solar heat collecting tube 7 converts solar energy into heat energy, heat a heat exchange medium inside the solar heat collecting tube 7, the heat exchange tube 2 is assembled in the evaporation chamber 3, the control box 6 controls the operation of a medium water pump 63 inside the solar heat collecting tube 7, so that a high-temperature heat exchange medium inside the solar heat collecting tube 7 circulates between the heat exchange tube 2 and the solar heat collecting tube 7, the surface temperature of the heat exchange tube 2 is improved, the seawater is atomized into micron-sized particles by the electrostatic atomization device 4, the atomized seawater charged droplets are adsorbed on the surface of the heat exchange tube 2 and heated and evaporated under the action of a high-voltage electrostatic field, the condensation chamber 1 is installed above the evaporation chamber 3, and.
The specific structure of each device in this embodiment is as follows:
referring to fig. 1 and 2, the electrostatic atomization device 4 includes a needle 41, a needle support 42, a mounting base 43, a base support 44, and a water inlet pipe 45. The spray needles 41 are connected with a water inlet pipe 45 through tee quick connectors, the tee quick connectors are embedded into the spray needle support 42 and fixed in a groove, the four spray needles 41 are of a symmetrical structure by taking the water inlet pipe as the center, all pipelines are kept on the same plane, the flow rate of each spray needle 41 is kept consistent, and then the high-voltage electrostatic field is enabled to tend to be in a stable state, so that charged liquid drops after atomization of each spray needle 41 can be uniformly adsorbed on the heat exchange pipe 2. The spray needle support 42 is made of a non-metal material with good insulating property, and the whole structure is fixed on the mounting base 43 by threads; base support 44 is made of a non-metallic material with good insulating property, and is integrally fixed below installation base 43, the area of base support 44 is smaller than that of installation base 43, and accumulated water on installation base 43 is prevented from being connected with seawater water storage tank 5 through base support 44, so that an insulating effect is achieved.
Referring to fig. 1 and 4, the control box 6 is placed on the side of the evaporation chamber 3 and locked with the side of the evaporation chamber 3 through threads, and mainly comprises a high-pressure generator 61, a seawater pump 62, a medium pump 63, a sensor 64 and a central controller 65. The devices in the control box 6 are connected with a power supply, the power supply provides power for the devices, the sensor 64 is a temperature sensor, the model of the sensor 64 is a PT100 temperature probe, the central controller 65 is connected with the seawater pump 62, the medium pump 63 and the sensor 64, and the model of the central controller 65 is an SEMEM DV34 type intelligent controller.
The anode of the high-voltage generator 61 is connected with the spray needles 41 through leads, the cathode of the high-voltage generator 61 is connected with the heat exchange tube 2, a high-voltage electrostatic field of 8-12 KV is formed, the distance between two side surfaces of the heat exchange tube 2 and the inner wall of the nearest evaporation chamber 3 is 5 cm, and the four spray needles 41 are respectively located in the middle areas between the two side surfaces of the heat exchange tube 2 and the inner wall of the evaporation chamber 3. The heat exchange tube 2 is placed right above the installation base 43 of the electrostatic atomization device 4, the vertical distance between the top ends of the spray needles 41 and the heat exchange tube 2 is 5 centimeters, and meanwhile, the four spray needles 41 are shifted to be inwardly deviated by 5 degrees, so that the atomization effect is optimal, and under the action of a high-voltage electrostatic field, seawater sprayed from the ends of the spray needles 41 is atomized into micron-sized fine particles which are uniformly adsorbed on the heat exchange tube 2. The sensor 64 collects the temperature of the heat exchange tube 2 in real time, the central controller 65 receives data of the sensor 64 through a serial port, when the temperature in the heat collection tube 7 is higher than 60 ℃, the high-pressure generator 61 and the seawater pump 62 are started to work, and the voltage value of the high-pressure generator 61 and the flow rate of the seawater pump 62 are adjusted according to the change of the temperature value. The water inlet of the seawater pump 62 is connected with the seawater storage tank 5 through a water pipe, the water outlet is connected with the water inlet pipe 45 of the electrostatic atomization device through a water pipe, and when the seawater pump 62 works, seawater is pumped from the seawater storage tank 5 and is sprayed out through the spray needles 41; the water inlet of the medium water pump 63 is connected with the heat collecting pipe 7, the water outlet of the medium water pump is connected with the water inlet of the heat exchange pipe 2, the water outlet of the heat exchange pipe 2 is connected back to the heat collecting pipe 7 through the water pipe, and when the heat collecting pipe works, a heat exchange medium heated by the heat collecting pipe 7 continuously circulates between the heat exchange pipe 2 and the heat collecting pipe 7 under the action of the medium water pump 63.
Referring to fig. 1, 2 and 3, the condensing chamber 1 mainly comprises a condensing chamber main body 15 and a condensing chamber top cover 11; the four sides in the condensation chamber main body 15 contain fresh water collecting grooves 16 with the width of 10 centimeters, and water vapor is condensed into required fresh water on the top cover 11 of the condensation chamber and the inner wall of the condensation chamber main body 15 and stored in the fresh water collecting grooves 16; the fresh water collecting pipe 17 is flush with the lower surface of the condensation chamber main body 15; the condensing chamber top cover 11 comprises a water spraying pipe 12, water storage tank pieces 13 and a flow guide pipe 14, wherein the water storage tank pieces 13 are arranged perpendicular to the condensing chamber top cover 11; the seawater pump 62 of the control box 6 supplies water to the water spraying pipe 12, the water spraying pipe 12 is provided with small holes, seawater passing through the water spraying pipe 12 flows into the water storage tank piece 13 through the small holes, an included angle of 15-30 degrees is formed between the top cover 11 of the condensation chamber and the horizontal plane, so that the condensation area is increased, and meanwhile, condensed water on the top cover 11 of the condensation chamber slides to the fresh water collecting tank 16 along the inclined plane; the valve of the collecting pipe 17 is opened, so that fresh water can be collected; meanwhile, the guide pipe 14 of the condensing chamber top cover 11 is connected with the seawater water storage tank 5 through a water pipe, seawater flowing through the condensing chamber top cover 11 absorbs heat when accelerating the condensation of seawater and flows back to the seawater water storage tank 5 through the guide pipe 14, secondary utilization of energy is achieved, and the utilization rate of the energy is improved.
The detailed description of the present embodiment is as follows:
the solar heat collecting tube 7 converts solar energy into heat energy, heat a heat exchange medium in the heat collecting tube 7, the heat exchange tube 2 is assembled in the evaporation chamber 3, a medium water pump 63 controls a high-temperature heat exchange medium in the heat collecting tube 7 to circulate between the heat exchange tube 2 and the heat collecting tube 7, the surface temperature of the heat exchange tube 2 is improved, the electrostatic atomization device 4 atomizes seawater into micron-sized particles, atomized seawater charged droplets are adsorbed on the surface of the heat exchange tube 2 and heated to evaporate under the action of a high-voltage electrostatic field, and evaporated water vapor rises to the condensation chamber 1 to be condensed to obtain fresh water;
the positive and negative ends of the high-voltage generator 61 are respectively connected with the spray needle 41 and the heat exchange tube 2 through leads; the sensor 64 collects the temperature of the heat exchange tube 2 in real time, the central controller 65 receives data of the sensor 64 through a serial port, when the temperature in the heat collection tube 2 is higher than 60 ℃, the high-pressure generator 61 and the seawater pump 62 are started to work, and the voltage value of the high-pressure generator 61 and the flow rate of the seawater pump 62 are adjusted according to the change of the temperature value.
The anode of the high-voltage generator 61 is connected with the spray needle 41 through a lead, the cathode of the high-voltage generator 61 is connected with the heat exchange tube 2 to form a high-voltage electrostatic field, so that seawater is atomized, the seawater pump extracts seawater from the seawater water storage tank 5 and sprays the seawater from the spray needle 41 through the water inlet tube 45, all pipelines are kept on the same plane, the seawater particles atomized by the spray needle 41 are distributed more uniformly in the space, atomized charged liquid drops can be adsorbed on the heat exchange tube 2 more uniformly, and the heat absorption is more sufficient;
when the electrostatic atomization device 4 works, seawater atomization liquid drops are filled between the heat exchange tube 2 and the four walls of the evaporation chamber 3, and the heat of the heat exchange tube 2 has more sufficient time to act on the atomized seawater liquid drops, so that the seawater liquid drops cannot be scattered through the outer wall of the evaporation chamber;
the water vapor is condensed into required fresh water on the top cover 11 of the condensing chamber and the inner wall of the main body 15 of the condensing chamber and stored in the fresh water collecting tank 16; the water that condenses on the condensation chamber top cap 11 can slide along the inclined plane and arrive fresh water collecting vat 16, and self heat absorption when the normal atmospheric temperature sea water that flows through on the condensation chamber top cap 11 acceleratees the high temperature sea water of condensation is flowed back to sea water storage box 5 through honeycomb duct 14, realizes the second grade utilization to the energy, improves energy utilization.
The foregoing shows and describes the general principles, essential features, and advantages of the invention. It will be understood by those skilled in the art that the present invention is not limited to the above embodiments, and that the principles of the present invention may be applied to any other embodiment without departing from the spirit and scope of the present invention. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (8)
1. A small split solar electrostatic atomization seawater desalination device comprises a solar heat collecting pipe, a seawater water storage tank, an electrostatic atomization device, an evaporation chamber, a heat exchange pipe and a condensation chamber, and is characterized in that the heat exchange pipe is assembled in the evaporation chamber, the seawater water storage tank is positioned at the bottom of the evaporation chamber, the electrostatic atomization device is positioned at the top of the seawater water storage tank and below the heat exchange pipe, and the condensation chamber is positioned at the top of the evaporation chamber and communicated with the evaporation chamber;
a medium water pump is arranged between the heat exchange tube and the solar heat collection tube, a water inlet of the medium water pump is connected with the solar heat collection tube, a water outlet of the medium water pump is connected with a water inlet of the heat exchange tube, a water outlet of the heat exchange tube is connected back to the solar heat collection tube through a water pipe, and a heat exchange medium circulates between the heat exchange tube and the solar heat collection tube through the.
2. The small split solar electrostatic atomization seawater desalination device of claim 1, wherein the electrostatic atomization device comprises a spray needle, a spray needle support, a mounting base, a base support and a water inlet pipe; the spray needle is connected with the water inlet pipe through a tee joint quick connector, the head of the spray needle extends into the evaporation chamber, the quick connector is embedded into a groove of the spray needle support for fixation, the spray needle support is fixed on the mounting base through threads, and the base support is placed below the mounting base; the area supported by the base is smaller than that of the mounting base.
3. The small split solar electrostatic atomization seawater desalination device of claim 2, wherein the pipelines of the water inlet pipe are kept on the same plane, and four spray needles of the electrostatic atomization device are arranged in a symmetrical structure with the water inlet pipe as the center.
4. The small split solar electrostatic atomization seawater desalination device of claim 2, which is characterized by further comprising a control box, wherein the control box is placed on the side surface of the evaporation chamber and is locked with the side surface of the evaporation chamber through threads, the control box comprises a high-pressure generator, a seawater pump, a medium pump, a sensor and a central controller, and the positive end and the negative end of the high-pressure generator are respectively connected with the spray needle and the heat exchange tube through leads; the sensor is attached to the heat exchange tube, the central controller is communicated with the sensor through a serial port, the seawater pump is connected with the seawater water storage tank and the water inlet tube of the electrostatic atomization device through a guide tube, and the medium water pump is connected with the solar heat collection tube and the heat exchange tube through a guide tube.
5. The small-sized split solar electrostatic atomization seawater desalination device of claim 3, wherein the heat exchange tube is positioned in the center of the evaporation chamber, two side surfaces of the heat exchange tube are 5 cm away from the inner wall of the nearest evaporation chamber, and four spray needles are respectively positioned in the middle areas of the two side surfaces of the heat exchange tube and the inner wall of the evaporation chamber; the heat exchange tube is placed right above the mounting base of the electrostatic atomization device, the vertical distance between the top ends of the spray needles and the heat exchange tube is 5 cm, and meanwhile, the four spray needles are inwardly deviated by 5 degrees.
6. The small split solar electrostatic atomization seawater desalination device of claim 4, wherein the condensation chamber comprises a condensation chamber main body and a condensation chamber top cover, four sides of the condensation chamber main body are provided with fresh water collecting tanks, the fresh water collecting tanks are connected with fresh water collecting pipes, and the fresh water collecting pipes are flush with the lower surface of the condensation chamber main body;
the top of condensing chamber top cap has trickle pipe, catch basin piece, honeycomb duct, and catch basin piece perpendicular to condensing chamber top cap is placed, through the sea water pump of control box supplies water for the trickle pipe, and it has the aperture to open on the trickle pipe, and the sea water through the trickle pipe can flow into the catch basin piece through the aperture, and the honeycomb duct is connected to the catch basin piece.
7. The small split solar electrostatic atomization seawater desalination device of claim 6, wherein the top cover of the condensation chamber forms an angle of 15-30 ° with the horizontal plane.
8. The small-sized split-type solar electrostatic atomization seawater desalination device of claim 6, wherein the flow guide pipe is connected with the seawater storage tank through a conduit, and the flow guide pipe exchanges heat with seawater in the seawater storage tank.
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| CN201920884529.2U CN210885391U (en) | 2019-06-13 | 2019-06-13 | Small split solar electrostatic atomization seawater desalination device |
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| CN201920884529.2U CN210885391U (en) | 2019-06-13 | 2019-06-13 | Small split solar electrostatic atomization seawater desalination device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110104715A (en) * | 2019-06-13 | 2019-08-09 | 东华理工大学 | A kind of small-sized separated type solar electrostatic atomization desalination plant and its method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110104715A (en) * | 2019-06-13 | 2019-08-09 | 东华理工大学 | A kind of small-sized separated type solar electrostatic atomization desalination plant and its method |
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Granted publication date: 20200630 Termination date: 20210613 |