CN108569740A - High-salt wastewater processing system based on solar energy - Google Patents
High-salt wastewater processing system based on solar energy Download PDFInfo
- Publication number
- CN108569740A CN108569740A CN201810469094.5A CN201810469094A CN108569740A CN 108569740 A CN108569740 A CN 108569740A CN 201810469094 A CN201810469094 A CN 201810469094A CN 108569740 A CN108569740 A CN 108569740A
- Authority
- CN
- China
- Prior art keywords
- solar energy
- processing system
- waste water
- salt wastewater
- reative cell
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
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- 239000002351 wastewater Substances 0.000 title claims abstract description 59
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 28
- 239000010959 steel Substances 0.000 claims abstract description 28
- 238000009833 condensation Methods 0.000 claims abstract description 20
- 230000005494 condensation Effects 0.000 claims abstract description 20
- 230000011514 reflex Effects 0.000 claims abstract description 18
- 239000007921 spray Substances 0.000 claims abstract description 11
- 238000010521 absorption reaction Methods 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- 238000007789 sealing Methods 0.000 claims description 5
- 239000010865 sewage Substances 0.000 claims description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 238000005086 pumping Methods 0.000 abstract description 3
- 150000003839 salts Chemical class 0.000 description 12
- 230000009102 absorption Effects 0.000 description 9
- 230000000694 effects Effects 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 6
- 238000009834 vaporization Methods 0.000 description 6
- 230000008016 vaporization Effects 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000012528 membrane Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 239000012267 brine Substances 0.000 description 4
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 4
- 239000002689 soil Substances 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 241001424688 Enceliopsis Species 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000003245 coal Substances 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000002826 coolant Substances 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 230000003204 osmotic effect Effects 0.000 description 2
- 230000000737 periodic effect Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000006911 enzymatic reaction Methods 0.000 description 1
- 238000007701 flash-distillation Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/14—Treatment of water, waste water, or sewage by heating by distillation or evaporation using solar energy
-
- 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
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The high-salt wastewater processing system based on solar energy that the present invention relates to a kind of, including solar energy collection unit and treatment unit for waste water, the solar energy collection unit includes the solar panel of spherical crown shape, the inner surface of the solar panel has been plated in reflex reflector lens, the reflex reflector lens are plated in 120 pieces/square metre, and above the solar panel, heat collector is installed at the convergence of several reflex reflector lens reflected lights, the heat collector is connected to treatment unit for waste water；The treatment unit for waste water includes closed reative cell, steel plate, spray thrower and steam accumulator are provided, in sequence from bottom to top, in the reative cell, the steel plate is connected to heat collector by defeated heat pipe, the spray thrower is connected by pumping with the waste water source outside reative cell, and the steam accumulator is connected with vapour condensation device.The high-salt wastewater processing system based on solar energy that the present invention obtains is simple in structure, novel, solar energy can be made full use of to generate thermal energy, investment is small, efficient.
Description
Technical field
The present invention relates to technical field of waste water processing more particularly to a kind of high-salt wastewater processing systems based on solar energy.
Background technology
High-salt wastewater refers to the waste water of total saliferous mass fraction at least 1%, essentially from chemical plant and oil and naturally
Acquisition processing of gas etc..The way of production of brine waste is extensive, and water also increases year by year.High salinity waste water is according to production process
Difference, the type and chemical property of contained organic matter differ greatly, but contained salts substances are mostly Cl—、SO4 2—、Na+、Ca2+Deng
Salts substances.Although these ions are all nutrients necessary to microorganism growth, played in the growth course of microorganism
Promote enzyme reaction, maintain membrane equilibrium and adjusts the important function of osmotic pressure.But if these ion concentrations are excessively high, can be to microorganism
Inhibition and toxic action are generated, if salinity height can cause osmotic pressure high, to make microbial cell dehydration cause cell primary
Matter detaches；Salinity is high, and the density of waste water can be caused to increase, and activated sludge easily floats loss, to seriously affect biological treatment
The clean-up effect etc. of system.
Currently, the processing of brine waste is mainly evaporated and membrane technology based on, evaporation technique such as multiple-effect evaporation, more
Grade flash distillation, both vapor compression condensation, mechanical compression.Membrane technology such as membrane distillation, positive infiltration technology etc..Such as《Guangdong chemical industry》2013 18
The processing system of these types of waste water is just described in the article of application of the phase evaporative desalination technology in industrial wastewater
System and device.Although achieving certain effect in terms of brine waste processing, high operating cost and investment cost with
And the corrosion and scaling problem of equipment makes steam raising high-salt wastewater treatment technology be difficult to promote and apply.And use membrane technology to containing
Salt waste water, which is handled also, has the shortcomings that cost of investment is big, operating cost is high, often handles 1 ton of brine waste and just needs to spend
The operating cost of members up to a hundred, thus be not of practical significance for carrying out on a large scale.It is low thus how to seek a kind of operating cost
It is honest and clean, can long-term operation and convenient for generate it is pure can reuse water high-salt wastewater processing unit, be that the art is current
It is badly in need of completing for task.
Invention content
To solve the above-mentioned problems, the high-salt wastewater processing system based on solar energy that the present invention provides a kind of, this is based on
The high-salt wastewater processing system of solar energy is simple in structure, novel, solar energy can be made full use of to generate thermal energy, investment is small, efficient.
The technical solution adopted by the present invention is：A kind of high-salt wastewater processing system based on solar energy, including solar energy are received
Collection unit and the treatment unit for waste water that is connected with solar energy collection unit, the solar energy collection unit include spherical crown shape too
Positive energy collecting board, the inner surface of the solar panel have been plated in reflex reflector lens, and the reflex reflector lens are with 120 pieces/square metre
It is plated in, and heat collector is installed above the solar panel, at the convergence of several reflex reflector lens reflected lights,
The heat collector is connected to treatment unit for waste water；The treatment unit for waste water includes closed reative cell, in the reative cell from
Steel plate, spray thrower and steam accumulator are equipped on down successively, the steel plate is connected to heat collector, the spray by defeated heat pipe
Leaching device is connected by pumping with the waste water source outside reative cell, and the steam accumulator is connected with vapour condensation device.
It is further limited as to above-mentioned technical proposal, the solar panel bottom is provided with universal shaft, described
Solar panel is equipped with sun automatic tracking device.
It is further limited as to above-mentioned technical proposal, the heat collector includes the shell of stainless steel, in the shell
Portion has been evenly arranged multiple heat absorption columns.
It is further limited as to above-mentioned technical proposal, the heat absorption column is copper, iron or ore or high temperature superconducting materia
Absorb heat column.
It is further limited as to above-mentioned technical proposal, the vapour condensation device is the pipe that can carry out condensation process
Road, the pipeline extend to outside reative cell and buried in underground, and are connected with waste water far from steam accumulator end with pipeline and return
Closed cans.
It is further limited as to above-mentioned technical proposal, manhole is offered on the side wall of the reative cell.
It is further limited as to above-mentioned technical proposal, the bottom of the reative cell offers slag-drip opening, the deslagging
Mouth is equipped with sealing cover.
High-salt wastewater processing system of the present invention based on solar energy, it is several by being plated on solar panel
Sunray can be reflected and be converged at heat collector, the focusing ratio of light is so then remarkably improved, so as to have by reflex reflector lens
Effect by light energy collection and be converted into thermal energy, thus collecting efficiency can be effectively improved；Thermal energy can then be conveyed by defeated heat pipe
To the steel plate of reative cell, and make steel plate that can be heated to 1000 DEG C, thus high-salt wastewater be sprayed on steel plate after can moment
Vaporization, and salt contained in waste water can be precipitated and remain on steel plate, the vapor of vaporization, which subsequently enters vapour condensation device, to be obtained
To recycling.Thus, the high-salt wastewater processing system of the present invention based on solar energy can fully convert solar energy
Processing is evaporated to high-salt wastewater at thermal energy, thus can effectively reduce operating cost, and heat build-up is convenient, it is small using power,
Expense is low, and heat build-up is efficient, is not also limited by scale；Meanwhile the form that thermal energy is converted into using solar energy is also effective
The energy such as electricity, coal are saved, the pollution to environment is effectively reduced.
The setting of sun automatic tracking device of the present invention, can make solar energy collection unit automatic sun-tracking, to make
Solar energy collection unit is directed at sunlight and can be by solar energy reflection to heat collector always, thus solar energy can be made full use of to provide
Source.
Multiple heat absorption columns of heat collector inner homogeneous arrangement of the present invention, it is possible to increase endotherm area, so as to effectively carry
Highly endothermic efficiency.
It is embedded in condensation pipeline in underground in vapour condensation device of the present invention, the constant temperature ring of 10 DEG C of soil can be made full use of
Border carries out condensation process to steam, and condensation effect is good, and is not necessarily to coolant, can save enterprise's production cost.
The setting of manhole of the present invention periodically can clear up the salt being precipitated on steel plate convenient for staff, simultaneously
Can also periodic maintenance be carried out to steel plate.
The setting of slag-drip opening of the present invention, for being carried out at deslagging to the solid salt and impurity that fall to reative cell bottom
Reason,
Description of the drawings
Fig. 1 is the structural schematic diagram of the embodiment of the present invention；
In figure：1- solar absorption units；11- solar panels；12- reflex reflector lens；13- heat collectors；The defeated heat of 14-
Pipe；2- treatment unit for waste water；21- steel plates；22- spray throwers；23- steam collection hoods；3- pipelines；4- Sewage treatment tanks.
Specific implementation mode
Below in conjunction with the accompanying drawings and specific embodiment, the present invention is described in further details.
As shown in Figure 1, it includes solar energy collection unit 1 and and solar energy to be somebody's turn to do the high-salt wastewater processing system based on solar energy
Solar energy is collected and is converted into other work(by the connected treatment unit for waste water 2 of collector unit 1, such solar energy collection unit 1
Afterwards, work(can be exported to treatment unit for waste water to be evaporated processing to waste water.
The solar energy collection unit 1 includes the solar panel 11 of spherical crown shape, the solar panel 11 it is interior
Surface has been plated in reflex reflector lens 12, and the reflex reflector lens 12 are plated in 120 pieces/square metre, and in the solar energy collecting
11 top of plate is equipped with heat collector 13 at the convergence of 12 reflected light of several reflex reflector lens, and the heat collector 13 is connected to useless
Water treatment unit 2.In being plated in several reflex reflector lens 12 on solar panel 11, sunray can be reflected and converge at heat build-up
At device, it is so then remarkably improved the focusing ratio of light, so as to effectively by light energy collection and be converted into thermal energy, thus can be effective
Improve collecting efficiency.In actual production, the reaction eyeglass 12 that a waste water needs 200 square metres is handled, therefore, according to reality
The case where required processing wastewater flow rate, can be configured the area of solar panel 11 and 12 quantity of reflex reflector lens being plated in.
The treatment unit for waste water 2 includes closed reative cell, be provided, in sequence from bottom to top, in the reative cell steel plate 21,
Spray thrower 22 and steam accumulator 23, the steel plate 21 are connected to heat collector 13 by defeated heat pipe 14, in this way, steel plate 21 is poly-
It can be heated to 1000 DEG C under the thermal energy that hot device 13 is collected.The spray thrower 22 is connected by pumping with the waste water source outside reative cell,
The waste water of waste water source can be sprayed on through spray thrower 22 on steel plate 21 in this way.Because steel billet temperature is higher, so high-salt wastewater is sprayed
After on steel plate 21 can instant vaporization, and salt contained in waste water can be precipitated and remain on steel plate 21.The vapor of vaporization with
After can be collected by steam accumulator 23.The steam accumulator 23 is connected with vapour condensation device.In this way, vapor can be through steam
Collector 23, which enters in vapour condensation device, is condensed into water, to realize recycling.
Specifically, the vapour condensation device is the pipeline 3 that can carry out condensation process, the pipeline 3 extends to reative cell
It is external and buried in underground, and it is connected with Sewage treatment tank 4 far from 23 end of steam accumulator in pipeline 3, it is cold in pipeline 3 in this way
Solidifying water can be flowed into Sewage treatment tank 4 and be kept in.Pipeline 3 is embedded in the condensation process that underground carries out vapor, is because of soil
It is a good insulating layer, no matter how atmospheric temperature changes, and is all the environment of an opposite constant temperature in soil, can so fill
Point water vapour is condensed using the isoperibol of 10 DEG C of soil, condensation effect is good, and is not necessarily to coolant, effectively save can look forward to
Industry production cost.
11 bottom of the solar panel is provided with universal shaft, and the solar panel 11 is automatic equipped with the sun
Tracker.The setting of sun automatic tracking device can make 1 automatic sun-tracking of solar energy collection unit, to make solar energy collecting
Unit 1 is directed at sunlight and can be by solar energy reflection to heat collector 13 always, thus can make full use of solar energy resources.And it is universal
The setting of axis can then be such that solar panel is rotated automatically under universal shaft effect, can effectively save labour, also avoid work
Make the hardship of exposure of the personnel under the sun.
Further, the heat collector 13 includes the shell of stainless steel, and the enclosure interior has been evenly arranged multiple heat absorptions
Column.The heat absorption column is copper, iron or ore or high temperature superconducting materia heat absorption column.Multiple heat absorptions of 13 inner homogeneous of heat collector arrangement
Column, it is possible to increase endotherm area, so as to effectively improve heat absorption efficiency.In this way,
In addition, offering manhole on the side wall of the reative cell.The setting of manhole can be convenient for staff periodically to steel plate
The salt of upper precipitation is cleared up, while can also carry out periodic maintenance to steel plate.The bottom of the reative cell is further opened with slag-drip opening,
The slag-drip opening is equipped with sealing cover.The setting of slag-drip opening can be used for the solid salt to falling to reative cell bottom and impurity progress
Deslagging processing, prevents reative cell bottom from influencing the normal use of reative cell there are excessive solid salt or impurity.When needs pair
When reative cell carries out deslagging, opening the sealing cover of slag-drip opening can be operated；After the completion of deslagging operation, again by sealing cover
It is placed on slag-drip opening, to ensure the leakproofness of reative cell.
When in use, sunray is irradiated in solar energy collecting to the high-salt wastewater processing system based on solar energy of the present invention
At the reflex reflector lens 12 that 11 top of plate is plated in, and light is converged at heat collector 13 under the effect of reflex reflector lens 12, by light
It can be converted into thermal energy, the thermal energy at subsequent heat collector 13 is delivered continuously to through defeated heat pipe 14 at the steel plate 21 in reative cell, makes steel
Plate 21 is heated to 1000 DEG C, thus high-salt wastewater after being sprayed on steel plate through spray thrower 22 can instant vaporization, and in waste water
Contained salt can be precipitated and remain on steel plate, and the vapor of vaporization is then sharp again into vapour condensation device progress condensing recovery
With.After running a period of time, the salt being precipitated on steel plate can be cleared up by the manhole on reative cell, thus can effectively kept away
Exempting from salt amount on steel plate excessively influences its normal use.High-salt wastewater processing system of the present invention based on solar energy, can
Thermal energy is fully converted solar energy into be evaporated processing to high-salt wastewater, thus can effectively reduce operating cost, and heat build-up
Convenient, small using power, expense is low, and heat build-up effect is good, is not also limited by scale；Meanwhile it being converted into using solar energy
The form of thermal energy also effectively saves the resources such as electricity, coal, effectively reduces the pollution to environment.
The foregoing is merely better embodiments of the present invention, but scope of protection of the present invention is not limited thereto, any ripe
Know those skilled in the art in the technical scope disclosed by the present invention, the technique according to the invention design be subject to equivalent replacement or
The technical solution for changing gained, should all be covered by protection scope of the present invention.
Claims (7)
1. a kind of high-salt wastewater processing system based on solar energy, it is characterised in that：Including solar energy collection unit and and the sun
The connected treatment unit for waste water of energy collector unit, the solar energy collection unit includes the solar panel of spherical crown shape, described
The inner surface of solar panel has been plated in reflex reflector lens, and the reflex reflector lens are plated in 120 pieces/square metre, and in institute
It states above solar panel, heat collector, the heat collector connection is installed at the convergence of several reflex reflector lens reflected lights
To treatment unit for waste water；The treatment unit for waste water includes closed reative cell, is provided, in sequence from bottom to top, in the reative cell
Steel plate, spray thrower and steam accumulator, the steel plate are connected to heat collector by defeated heat pipe, and the spray thrower is by pump and instead
Outdoor waste water source is answered to be connected, the steam accumulator is connected with vapour condensation device.
2. the high-salt wastewater processing system according to claim 1 based on solar energy, it is characterised in that：The solar energy is received
Collection board bottom portion is provided with universal shaft, and the solar panel is equipped with sun automatic tracking device.
3. the high-salt wastewater processing system according to claim 1 based on solar energy, it is characterised in that：The heat collector packet
The shell of stainless steel is included, the enclosure interior has been evenly arranged multiple heat absorption columns.
4. the high-salt wastewater processing system according to claim 3 based on solar energy, it is characterised in that：The heat absorption column is
Copper, iron or ore or high temperature superconducting materia heat absorption column.
5. the high-salt wastewater processing system according to claim 1 based on solar energy, it is characterised in that：The steam condensation
Device is the pipeline that can carry out condensation process, and the pipeline extends to outside reative cell and buried in underground and separate in pipeline
Steam accumulator end is connected with Sewage treatment tank.
6. the high-salt wastewater processing system according to claim 1 based on solar energy, it is characterised in that：The reative cell
Manhole is offered on side wall.
7. the high-salt wastewater processing system according to claim 1 based on solar energy, it is characterised in that：The reative cell
Bottom offers slag-drip opening, and the slag-drip opening is equipped with sealing cover.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810469094.5A CN108569740A (en) | 2018-05-16 | 2018-05-16 | High-salt wastewater processing system based on solar energy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810469094.5A CN108569740A (en) | 2018-05-16 | 2018-05-16 | High-salt wastewater processing system based on solar energy |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108569740A true CN108569740A (en) | 2018-09-25 |
Family
ID=63572617
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810469094.5A Pending CN108569740A (en) | 2018-05-16 | 2018-05-16 | High-salt wastewater processing system based on solar energy |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111715076A (en) * | 2020-06-11 | 2020-09-29 | 江南大学 | Air energy vacuum membrane distillation device and distillation method |
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|---|---|---|---|---|
| CN101921006A (en) * | 2010-06-09 | 2010-12-22 | 深圳市环境工程科学技术中心 | Integrated concentrating solar power and seawater desalination method and system |
| CN106745434A (en) * | 2017-03-31 | 2017-05-31 | 云南师范大学 | A kind of operation under positive pressure desalting seawater through multi-effect evaporation system based on the middle temperature heat build-up of solar energy |
| US20170355617A1 (en) * | 2016-06-13 | 2017-12-14 | Qi Wang | Counter circulating liquid processing system by repeatedly re-using thermal energy |
| CN208378467U (en) * | 2018-05-16 | 2019-01-15 | 河北格源环保科技有限公司 | High-salt wastewater processing system based on solar energy |
-
2018
- 2018-05-16 CN CN201810469094.5A patent/CN108569740A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101921006A (en) * | 2010-06-09 | 2010-12-22 | 深圳市环境工程科学技术中心 | Integrated concentrating solar power and seawater desalination method and system |
| US20170355617A1 (en) * | 2016-06-13 | 2017-12-14 | Qi Wang | Counter circulating liquid processing system by repeatedly re-using thermal energy |
| CN106745434A (en) * | 2017-03-31 | 2017-05-31 | 云南师范大学 | A kind of operation under positive pressure desalting seawater through multi-effect evaporation system based on the middle temperature heat build-up of solar energy |
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| Title |
|---|
| 潘玉勤主编；杜永恒副主编: "水/土壤源热泵地下换热***施工技术手册》", vol. 1, 29 February 2016, 黄河水利出版社, pages: 3 - 4 * |
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Cited By (1)
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| CN111715076A (en) * | 2020-06-11 | 2020-09-29 | 江南大学 | Air energy vacuum membrane distillation device and distillation method |
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