CN201567245U - Device utilizing solar energy to desalinating seawater and producing salt - Google Patents
Device utilizing solar energy to desalinating seawater and producing salt Download PDFInfo
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- CN201567245U CN201567245U CN2009201511757U CN200920151175U CN201567245U CN 201567245 U CN201567245 U CN 201567245U CN 2009201511757 U CN2009201511757 U CN 2009201511757U CN 200920151175 U CN200920151175 U CN 200920151175U CN 201567245 U CN201567245 U CN 201567245U
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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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- 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
Abstract
The utility model discloses a device taking solar energy as the energy source to desalinating seawater and producing salt. The device includes a solar energy thermal collector, an evaporator, a thermal transducer, a salt settling tank, as well as pipelines for connecting each part, valves and pumps; the device utilizes the solar energy thermal collector to provide thermal source to the evaporator and simultaneously provide steam to drive a steam turbine to generate electricity; cold seawater adsorbed into the thermal transducer is heated and then sent into the evaporator; the secondary steam generated by the evaporator is sent into a steam compression machine to be compressed and heated, and then is recycled and enters the evaporator; and desalinated condensate water is generated in the evaporator and sent into the thermal transducer to be used for heating the cold seawater; and supersaturated brine and saturated brine generated by the evaporator are sent into the salt settling tank of a crude salt collection tank. The utility model further provides a steam boiler.
Description
Technical field
The utility model relates to the device of sea water desaltination, and particularly a kind of sun power that utilizes carries out sea water desaltination for the energy, and can produce the device of salt simultaneously.In device of the present utility model, be provided with solar energy collector, vaporizer, interchanger, salt settling groove, and the pipeline, valve and the pump that connect each several part.
Background technology
Along with the raising of socioeconomic sustained and rapid development and living standards of the people, shortage of water resources and water pollution problems become increasingly conspicuous, and seek the important topic that new water source and water saving become current society.It is an ancient problem to obtain fresh water that seawater is desalinated processing, is again a focus of current era primary study simultaneously.
Traditional sea water desaltination is to adopt the multi-step evaporator group to distill processing, need to consume a large amount of steam, and terminal steam often can not directly utilize, and the part heat is wasted, it also wants the additive decrementation certain energy in order to handle cooling, and the thermo-efficiency utilization is not high.Because the consumer number is huge, electric power that supporting power consumes is also very huge, causes that system's floor space is big, cost of investment is high.Simultaneously, the useful resources in the seawater---sea salt also can not get effective utilization.
Chinese invention patent application 200610111779.X discloses a kind of temperature-differential sea-water distillator, it is a difference of utilizing the saturated vapor pressure of water vapor under the differing temps, at first seawater is heated, improve the dividing potential drop of saturated vapor, reduce temperature at condensing chamber then,, separate out pure water along with the reduction of saturated vapor dividing potential drop, according to this principle design one the cover desalting equipment, it comprises sea water tank, well heater, high-pressure hydraulic pump, spray chamber, condensing chamber, fresh-water tank and blower fan; Sea water tank is connected with well heater by pipeline, and the seawater of process well heater enters high-pressure hydraulic pump, and high-pressure hydraulic pump is connected with spray chamber, and spray chamber is connected with condensing chamber by pipeline, and condensing chamber is connected with fresh-water tank, and blower fan is connected with spray chamber by the spray chamber blast inlet.Mention its type of heating in this patent application especially and can adopt electrically heated mode, the heat energy heating that also can adopt solar heating or utilize engine radiator to emit utilizes sun power to realize sea water desaltination.But the desalination efficient of this method can be too not high.
Chinese invention patent application 01127319.4 open solar energy sea water desalting equipment and method.With water pump the seawater in the drainage well being sent into the solar heating pond heats up, behind the chimney filter secondary filtration, send into distillation tower again and carry out low-pressure distillation, rely on roots blower that it is under low pressure evaporated simultaneously, the water vapor that is drawn out of pressurization cools off through the cooling plate that pipeline returns the heating bath left end again, and flow out from the fresh water water outlet along the contrary seawater approach axis of the curve cooling tube of heating bath, therebetween with an end in heating bath, the other end replenishes evaporation institute heat requirement at the heating unit of many heat pipes of distillation tower bottom, and be provided with auger in the bottom of distillation tower and go out the salt device, comprehensive utilization makes the desalination water cost extremely low.
Chinese invention patent application 200810071554.5 discloses a kind of sun power embrane method method for desalting seawater and suite of equipment, and it is made of solar-energy photo-voltaic cell system, sea water preprocessing system and impervious desalination system three parts.The solar-energy photo-voltaic cell system comprises solar battery panel, framework, is arranged at the back side member at the solar battery panel back side and the store battery and the current converter composition of stored electric energy.The energy is provided for sea water preprocessing system and impervious desalination system by the solar-energy photo-voltaic cell system.Seawater is removed marine alga, planktonic organism, suspended substance, colloid, bacterium through the sea water preprocessing system handles, pump into reverse osmosis then, get fresh water and bittern (condensed water) through reverse osmosis desalination.But present stage, the efficient of solar photocell was lower, not only efficient is not high and adopt the reverse osmosis method to carry out the desalination of water, therefore and its water consumption is also very big, and needed energy consumption is higher, make only utilize sun power as the energy of this patent application technical scheme be close to become impossible.
The solar energy sea water desalination apparatus of China's utility model patent 200820054546.5 disclosed internal recycle multiple-effect evaporation condensations comprises solar energy collector, evaporator tower and condensing tower, described evaporator tower and condensing tower place in the integrated housing, and both epicoeles are communicated with by a blower fan, and cavity of resorption is communicated with by a ventage; A high-order hot water storage tank is arranged, and the import and export of described solar energy collector are communicated with the upper and lower cavity of high-order hot water storage tank respectively; A brinepump import is communicated with the cavity of resorption of evaporator tower, and outlet is connected the solar energy collector import respectively by valve and high-order hot water storage tank epicoele.But still there is inefficiency in this device, the deficiency that the energy is higher.
Disclosed technology from Chinese patent is gone back common deficiency of ubiquity in the prior art, promptly realizing sea water desaltination and fresh water also being taken away part energy in the discharge from system or device, energy can not fully be utilized.
Summary of the invention
The utility model provides that a kind of to overcome prior art insufficient jointly, the higher-energy utilising efficiency can be arranged, the device that can realize only depending on the energy of the sun to carry out sea water desaltination basically, and device of the present utility model can also be produced sea salt when desalinizing seawater.
Solar energy sea water desalination apparatus of the present utility model comprises solar energy collector, vaporizer, interchanger, salt settling groove, and the pipeline, valve and the pump that connect each several part.Wherein the Mare Frigoris water inlet of interchanger is connected with the seawater vacuum primingpump, the warm seawater liquid outlet of interchanger is connected with the fluid inlet of vaporizer, the secondary steam outlet of vaporizer is connected with the inlet of vapour compressor, the delivery port of vapour compressor is connected with the steam-in of vaporizer, obviously the vaporizer in the utility model is a vapour compression recirculation vaporizer, the desalination condensation-water drain of vaporizer is connected with the desalination heat of condensation mouth of a river of interchanger by desalination condensation water pot, the desalination condensation warm water outlet of interchanger links to each other with desalination water of condensation collection tube, the circulation fluid outlet of vaporizer is connected with the input aperture of vaporizer recycle liquid pump, the delivery port of recycle pump is connected with the circulation fluid of vaporizer inlet, the supersaturated brine outlet of vaporizer is connected with the input aperture of saturated brine Pump for giving-out, the delivery port of saturated brine Pump for giving-out connects the super dope jar of seawater, and saturated salt water pot connecting band has the salt settling groove of saturated brine outlet and crude salt receiving tank.Solar energy collector heating heat pipe, by heat pipe heat is passed to its internal recycle water and reaches boiling point, steam driven steam turbine power generation in the vapor can generation, the electric power that is sent is used for pump and the compressor work in the drive unit, also have pipeline to be communicated with vaporizer on the vapor can, this pipeline is provided with by-pass valve control.
Be seawater to be introduced the interchanger internal heating through the Mare Frigoris water inlet of interchanger in the utility model work by the seawater vacuum primingpump, seawater after the heating is admitted to heating once more in the vapour compression recirculation vaporizer, and seawater is played circulation by the vaporizer recycle pump, heating circulates, and the secondary steam that produces in the vaporizer is admitted to and is compressed in the vapour compressor, steam is by vapour compressor (heat pump) mechanical work, utilize reverse carnot's working cycle mode to work, from absorbing heat the low temperature environment on every side, heat is delivered to high-temperature medium (steam) by cryogenic object, formation has the acquisition elevated pressures, the steam of temperature and enthalpy, these steam are sent into vaporizer once more as the heating thermal source, seawater in the heating fumigators, the fresh water that the back forms of being condensed is then sent in the interchanger heating thermal source as interchanger by desalination water of condensation Pump for giving-out, be further cooled after the heat exchange in interchanger, cooled desalination water of condensation is discharged device of the present utility model by the fresh water collection tube, the bottom of vaporizer is provided with salt loading degree proofing unit, seawater in detecting vaporizer is about to supersaturated brine and sends in the super dope jar of seawater when becoming supersaturated brine, in seawater hyperconcentration jar, add an amount of salt kind crystalline substance and can make supersaturated brine induce rapid crystallization down to separate out sea salt, form thick crystallization at it.Send in the salt settling groove containing the super dope of crystalline, under the effect of stirring rake, can obtain byproduct---crude salt, and top stream obtains the saturated sea brine that contains and can obtain crude salt after further dehydration from underflow.Be provided with heat pipe in the solar energy collector in the utility model device, the heat that solar energy collector obtained transmits by heat pipe and produces the steam turbine that is used to drive generator work in the vapor can, and the electric power that is sent by generator is used for pump and the compressor work in the drive unit.The steam of vapor can generation simultaneously also can be sent into vaporizer, the thermal source of vaporizer during as the device initialization.
In the preferred embodiment of the present utility model, be connected with desalination condensation water pot 6 and desalination water of condensation Pump for giving-out 7 at the desalination condensation-water drain 36 of vaporizer 17 and 31 at the desalination heat of condensation mouth of a river of interchanger 8, between the steam-in 37 of the delivery port of vapour compressor 3 and vaporizer 17, be provided with steam buffer tank 18, the steam output pipe of vapor can 13 is connected with the steam-in 37 of vaporizer 17 with the steam input pipe of steam turbine 11 respectively by Y-tube 24 and is connected, and is provided with valve 40 between the pipe connecting of Y-tube 24 and steam-in 37.Owing to be connected with desalination condensation water pot 6 at the desalination condensation-water drain 36 of vaporizer 17 and 31 at the desalination heat of condensation mouth of a river of interchanger 8 in the preferred embodiment of the present utility model, can make whole device that more stable water of condensation work output is arranged, steam from flash distillation can be used as supplemental heat source simultaneously, further improve the thermo-efficiency of system; And the pump of being located at before the condensation water pot 67 can overcome discrepancy in elevation lift and the interior resistance and the flow rate of liquid that increases in the interchanger of device, improves heat exchange efficiency, also is convenient to length apart from being delivered in the gathering system.The steam buffer tank that is provided with can make device have more stable steam work output to be admitted in the evaporating pot, makes device work more stable and efficient; Can easily the steam by the solar energy collector heating evaporation be sent to steam turbine and vaporizer respectively by a threeway and the valve that is arranged on the corresponding pipeline, both can reduce the consumption of pipeline, also control provides convenience to plant automation.
29 of Mare Frigoris water inlets at seawater vacuum primingpump 9 and interchanger 8 among the embodiment of the present utility model are serially connected with grade one filter at least, and in preferred embodiment of the present utility model, adopted one-level CD coarse filter and mutual placed in-line one-level CD fine filter, the planktonic organism in the seawater, algae and other solid impurity can be filtered fully by two-stage filtration and guarantee unit normal run.The CD strainer that the utility model has adopted paper industry to use especially.The advantage of CD strainer is to filter disk to arrange that at regular intervals the quantity that can install is more, can realize that in useful volume larger area filters, compact equipment, and the place takies little, and cost of investment is low; The material of water and solubility is discharged owing to the pressure effect enters into tubular shaft through filter cloth, other silt, algae etc. are filtered and are adsorbed on the CD dish, and the surface adsorption foreign material are removed by the device interior scraper, are collected into sludge sump after scraping, discharge by wash water valve, can realize the non-stop run process; Because disk is made circumferential motion with middle tubular axis, can play the effect of self-stip, can effectively prolong equipment washing cycle and work-ing life; Simultaneously, every disk by work alone, the filter cloth of certain number forms, the maintenance of equipment cost is low, dismounting and change is convenient.
Among the embodiment of the present utility model, the check point that detects salt concn can be set, the salt concn automatic detection device perhaps is installed in supersaturated brine outlet 35.Can provide the information of opening the saturated brine Pump for giving-out to device after adopting these technical measures.
At most preferred embodiment of the present utility model is that vapor can is communicated with a steam boiler, and formation can be by sun power and steam boiler respectively to the system of vapor can heat supply.The device that constitutes by present embodiment has adopted the additional energy of steam boiler as sun power, can work independently separately, can use hybrid power to produce steam again generates electricity, particularly can fully use existing resource at night or when overcast and rainy, utilize steam boiler to produce steam, to satisfy uninterrupted long time continuous working process, realize the rational Match of system capacity on time and space.
Description of drawings
Accompanying drawing 1 is the device synoptic diagram of an embodiment of the present utility model.
Accompanying drawing 2 is the CD filter structure schematic representation.
Accompanying drawing 3 is a filter cloth synoptic diagram in the CD strainer.
Embodiment
Form and principle of work below in conjunction with accompanying drawing detailed explanation device of the present utility model:
Among the embodiment of the present utility model that accompanying drawing 1 provides, sun power is by solar energy collector 12 collections and heat the heat pipe of being located in the heat collector 12, and then the recirculated water in the heat collector 12 of will flowing through is heated to boiling point, the recirculated water that reaches boiling point from solar energy collector 12 through entering the mouth 21 in vapor can 13, make jar 13 interior steam that produce, part recirculated water that replenishes and unevaporated recirculated water turn back to heat collector 13, formation self-circulation process through 22.Water in the evaporating pot 13 is heated and changes steam into after threeway 24 can be sent to electric turbine 11 and vaporizer 17 respectively.The quantity of steam of sending into vaporizer 17 can be by valve 40 controls.In the utility model device works better, electric turbine 11 sends electric power and sends into the relevant power device of the utility model through power transmitting device 14, also can be connected to the grid.Seawater suction pump 19 in the utility model device sucks seawater, filter through secondary CD strainer 10 and 16 and to carry out heating evaporation in the interchanger 8 after Mare Frigoris water inlet 29 is sent into, the hot sea water after being heated is through 32 outputs of hot sea water liquid outlet and evaporate in fluid inlet 41 is sent into vaporizer 17.The secondary steam of vaporizer 17 evaporation is through exporting 44 inlets of sending into vapour compressor 3, the compression of compressed machine 3 forms has the steam that obtains elevated pressures, temperature and enthalpy, the delivery port of compressed again machine 3 is fed back in the vaporizer 17 heating thermal source as vaporizer 17 hot sea water in to 17 again after through steam buffer tank 18 and is heated once more through steam-in 37, steam buffer tank 18 can make device have stable steam work output to be admitted in the evaporating pot, makes device work more stable and efficient.After the steam that produces in vaporizer 17 is condensed into fresh water, desalination condensation-water drain 36 through vaporizer 17 is sent in the interchanger 8 with the desalination condensation water pot 6 and the desalination heat of condensation mouth of a river 31, the fresh water of condensation heats the Mare Frigoris water that enters in it as the heating thermal source in interchanger 8, condensation fresh water is further cooled off, and in interchanger 8 outlet 30 of set desalination condensation warm water and coupled desalination water of condensation collection tube 15 discharge systems.And the pump of being located at before the condensation water pot 67 can overcome the discrepancy in elevation lift of interchanger 8 and the resistance in the device, can improve the flow rate of liquid in the interchanger, improves heat exchange efficiency, also is convenient to long distance and is delivered in the gathering system.Vaporizer 17 be heated but not the seawater of vaporization enter in the vaporizer recycle liquid pump 4 by circulation fluid outlet 38, and under the effect of recycle pump 4, sent back to the heating that circulates in the vaporizer 17 once more by circulation fluid inlet 39.In this course, seawater is concentrated gradually, when the proofing unit of the check point that is arranged at supersaturated brine outlet 35 detects seawater salt concn in the vaporizer 17 and becomes supersaturated brine greater than preset value, saturated brine Pump for giving-out 5 promptly is unlocked, supersaturated brine is sent in the super dope jar 19 of seawater, in seawater hyperconcentration jar 19, add an amount of salt kind crystalline substance and can make supersaturated brine induce rapid crystallization down to separate out sea salt, form thick crystallization at it.The super dope that contains crystal salt is sent in the salt settling groove 20, under the effect of stirring rake, obtain from underflow that byproduct---crude salt enters in the crude salt receiving tank 2, and top stream obtains the saturated sea brine that contains and can flow out through salt solution saturated solution outlet 1, obtain crude salt after further dewatering.Be also shown in from Fig. 1, vapor can 13 usefulness also are communicated with a steam boiler 45, and the steam that is produced by valve 46 control steam boilers 45 enters in the vapor can 13.Boiler 45 in the utility model preferably adopts stalk rice husk steam boiler, strengthened like this existing resource has been made full use of, and adopt the additional energy of stalk rice husk steam boiler as sun power, and can work independently, can use hybrid power to produce steam again and generate electricity.This system is when sunlight is abundant, fully collect sun power, utilize solar energy collector to produce the steam driven steam turbine power generation plenum system energy, carry out sea water desaltination and produce salt, when then existing resource fully being used at night or when overcast and rainy, utilize stalk rice husk steam boiler to produce steam,, realize the coupling of system capacity on time and space to satisfy uninterrupted long time continuous working process.
Fig. 2 and Fig. 3 are the CD filter structure schematic representations, and wherein: 47 is wash water valve, and 48 is sludge sump, and 49 is filter body, and 50 is hollow rotating shaft, and 51 are the filtrate inlet, and 52 is the CD filtering table, and 53 is filtrate outlet.Its principle of work is to keep certain pressure in the filtration phase, and after filtrate entered into the strainer die cavity, the material of water and solubility was discharged owing to the pressure effect enters into tubular shaft through filter cloth.Other silt, algae etc. are filtered and are adsorbed on the CD dish, are collected into sludge sump after scraping, and are discharged by wash water valve.Select filter cloth specification order number according to filtering needs, and be divided into thick, the smart filtration.
Claims (5)
1. solar seawater desalination and salt production device, comprise solar energy collector, vaporizer, interchanger, the salt settling groove, and the pipeline that connects each several part, valve and pump, the Mare Frigoris water inlet (29) that it is characterized in that interchanger in the device (8) is connected with seawater vacuum primingpump (9), the hot sea water liquid outlet (32) of interchanger (8) is connected with the fluid inlet (41) of vaporizer (17), the secondary steam outlet (44) of vaporizer (17) is connected with the inlet of vapour compressor (3), the delivery port of vapour compressor (3) is connected with the steam-in (37) of vaporizer (17), the desalination condensation-water drain (36) of vaporizer (17) is connected with the desalination heat of condensation mouth of a river (31) of interchanger (8) by desalination condensation water pot (6), the desalination condensation warm water outlet (30) of interchanger (8) links to each other with desalination water of condensation collection tube (15), the circulation fluid outlet (38) of vaporizer (17) is connected with the input aperture of vaporizer recycle liquid pump (4), the delivery port of recycle pump (4) is connected with the circulation fluid of vaporizer inlet (39), the supersaturated brine outlet (35) of vaporizer (17) is connected with the input aperture of saturated brine Pump for giving-out (5), the delivery port of saturated brine Pump for giving-out (5) connects the super dope jar of seawater (19), saturated salt water pot (19) connects the salt settling groove (20) that has saturated brine outlet (1) and crude salt receiving tank (2), solar energy collector (12) heating heat pipe, by heat pipe heat is passed to its internal recycle water and reaches boiling point, the steam driven steam turbine (11) that produces at vapor can (13) generates electricity, the electric power that is sent is used for pump and the compressor work in the drive unit, vapor can (13) also has pipeline to be communicated with vaporizer (17), and this pipeline is provided with by-pass valve control.
2. a kind of solar seawater desalination according to claim 1 and salt production device, it is characterized in that between the desalination heat of condensation mouth of a river (31) of the desalination condensation-water drain (36) of vaporizer (17) and interchanger (8), being connected with desalination condensation water pot (6) and desalinate water of condensation Pump for giving-out (7), between the steam-in (37) of the delivery port of vapour compressor (3) and vaporizer (17), be provided with steam buffer tank (18), the steam output pipe of vapor can (13) is connected with the steam-in (37) of vaporizer (17) with the steam input pipe of steam turbine (11) respectively by Y-tube (24) and is connected, and is provided with valve (40) between the pipe connecting of Y-tube (24) and steam-in (37).
3. a kind of solar seawater desalination according to claim 2 and salt production device is characterized in that being serially connected with one-level CD strainer at least between the Mare Frigoris water inlet (29) of seawater vacuum primingpump (9) and interchanger (8).
4. a kind of solar seawater desalination according to claim 3 and salt production device is characterized in that in supersaturated brine outlet (35) check point that detects salt concn being set.
5. according to claim 1 or 2 or 3 or 4 described a kind of solar seawater desalination and salt production devices, it is characterized in that vapor can (13) also is communicated with a steam boiler (45).
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| Application Number | Priority Date | Filing Date | Title |
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| CN2009201511757U CN201567245U (en) | 2009-05-07 | 2009-05-07 | Device utilizing solar energy to desalinating seawater and producing salt |
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| CN2009201511757U CN201567245U (en) | 2009-05-07 | 2009-05-07 | Device utilizing solar energy to desalinating seawater and producing salt |
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| CN201567245U true CN201567245U (en) | 2010-09-01 |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102874999A (en) * | 2011-07-12 | 2013-01-16 | 北大工学院绍兴技术研究院 | Sludge drying system utilizing waste heat |
| WO2014090118A1 (en) * | 2012-12-14 | 2014-06-19 | 青岛格兰德新能源有限公司 | Directional control valve, air compression subsystem, and integrated water utilization system |
| KR101620099B1 (en) * | 2014-11-19 | 2016-05-11 | 한국에너지기술연구원 | Distributed desalination system by mixing solar thermal and pyrolysis gasification energy |
| WO2016080702A1 (en) * | 2014-11-19 | 2016-05-26 | 한국에너지기술연구원 | Seawater desalination system using dual heat sources |
| CN106276977A (en) * | 2015-06-05 | 2017-01-04 | 王锦林 | Saltern evaporation of seawater desalination and recovery rainwater installation |
| CN111115932A (en) * | 2019-11-27 | 2020-05-08 | 昆明理工大学 | Non-focusing solar seawater or saline-alkali water desalting device |
| CN114249373A (en) * | 2021-12-28 | 2022-03-29 | 内蒙古工业大学 | Solar water desalination device and method based on tubular hydrophobic ceramic membrane |
| CN114314990A (en) * | 2022-01-19 | 2022-04-12 | 中国华能集团清洁能源技术研究院有限公司 | Photo-thermal coupling evaporation condensate water recovery system and water recovery method |
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2009
- 2009-05-07 CN CN2009201511757U patent/CN201567245U/en not_active Expired - Lifetime
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102874999A (en) * | 2011-07-12 | 2013-01-16 | 北大工学院绍兴技术研究院 | Sludge drying system utilizing waste heat |
| CN102874999B (en) * | 2011-07-12 | 2014-08-13 | 北大工学院绍兴技术研究院 | Sludge drying system utilizing waste heat |
| WO2014090118A1 (en) * | 2012-12-14 | 2014-06-19 | 青岛格兰德新能源有限公司 | Directional control valve, air compression subsystem, and integrated water utilization system |
| KR101620099B1 (en) * | 2014-11-19 | 2016-05-11 | 한국에너지기술연구원 | Distributed desalination system by mixing solar thermal and pyrolysis gasification energy |
| WO2016080707A1 (en) * | 2014-11-19 | 2016-05-26 | 한국에너지기술연구원 | Distributed seawater desalination system mixing solar heat and waste energy |
| WO2016080702A1 (en) * | 2014-11-19 | 2016-05-26 | 한국에너지기술연구원 | Seawater desalination system using dual heat sources |
| KR20160059711A (en) * | 2014-11-19 | 2016-05-27 | 한국에너지기술연구원 | Desalination system by using dual source energy |
| KR101672852B1 (en) | 2014-11-19 | 2016-11-16 | 한국에너지기술연구원 | Desalination system by using dual source energy |
| CN106276977A (en) * | 2015-06-05 | 2017-01-04 | 王锦林 | Saltern evaporation of seawater desalination and recovery rainwater installation |
| CN111115932A (en) * | 2019-11-27 | 2020-05-08 | 昆明理工大学 | Non-focusing solar seawater or saline-alkali water desalting device |
| CN114249373A (en) * | 2021-12-28 | 2022-03-29 | 内蒙古工业大学 | Solar water desalination device and method based on tubular hydrophobic ceramic membrane |
| CN114314990A (en) * | 2022-01-19 | 2022-04-12 | 中国华能集团清洁能源技术研究院有限公司 | Photo-thermal coupling evaporation condensate water recovery system and water recovery method |
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Assignee: Jiujiang Jiuzhou Energy-Saving Environmental Protection Engineering Co.,Ltd. Assignor: Zhang Peizhou Contract record no.: 2010360000065 Denomination of utility model: Solar-energy sea water desalination and salt production device Granted publication date: 20100901 License type: Exclusive License Record date: 20101230 |
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