CN206705876U - Clean energy resource desalinization and salt making system - Google Patents
Clean energy resource desalinization and salt making system Download PDFInfo
- Publication number
- CN206705876U CN206705876U CN201720125517.2U CN201720125517U CN206705876U CN 206705876 U CN206705876 U CN 206705876U CN 201720125517 U CN201720125517 U CN 201720125517U CN 206705876 U CN206705876 U CN 206705876U
- Authority
- CN
- China
- Prior art keywords
- unit
- electro
- desalting
- energy resource
- pipeline
- 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.)
- Active
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/33—Wastewater or sewage treatment systems using renewable energies using wind energy
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides a kind of clean energy resource desalinization and salt making system.The system includes clean energy resource generator unit, electro-desalting unit, reverse osmosis unit and salt manufacturing unit, and electro-desalting unit electrically connects with clean energy resource generator unit；The seawer outlet pipeline of electro-desalting unit is connected with the sea intake pipeline of reverse osmosis unit；The concentrated water outlet conduit with electro-desalting unit, the concentrated water outlet conduit of reverse osmosis unit are connected the concentrated water inlet pipeline of salt manufacturing unit respectively.It can be powered using clean energy resource generator unit to electro-desalting unit, the electrochemical desalting of electro-desalting unit is combined with the membrane separation technique of reverse osmosis unit, it is a kind of desalination technology of sustainable development, on the basis of efficiently desalinizing seawater, the problem of energy resource consumption in desalting process is high, strong brine discharge and cost is too high can effectively solve the problem that.Meanwhile the concentrated water separated can be handled using salt manufacturing unit, Nacl is prepared, further reclaims the salts resources in seawater.
Description
Technical field
Sea marine desalination field is the utility model is related to, in particular to a kind of clean energy resource desalinization and system
Salt system.
Background technology
Freshwater resources deficiency in the world, it has also become the problem of people are increasingly deeply concerned.Desalinization has become the solution whole world
The important channel of water resources crisis.
At present, Global Seawater desalination ten thousand stere of the daily output about 3500 or so, wherein 80% is used for drinking water, solves 1
The water supply problem of people more than hundred million, i.e., 1/50 population supplies drinking water by desalinization in the world.There is seawater desalting plant 1.3 ten thousand in the whole world
More, replacement and increment technique of the desalinization as freshwater resources, more and more paid attention to by many coastal states in the world；
The whole world directly uses sea water as the fresh water that annual about 6000 billion cubic meters of industry cooling water inventory or so instead of a large amount of preciousnesses
Resource；The whole world 50,000,000 tons of salt extraction, magnesium and more than 260 ten thousand tons of magnesia, 200,000 tons of bromine etc. from ocean every year.Desalinization needs
Big energy is wanted, so not high in not rich national economy benefit.
Desalination technology is exactly the technology by salt solution and moisture content point separation, there is more than ten kinds of method, most important bag at present
Sea water freeze method, electroosmose process, the way of distillation, hyperfiltration and ammonium carbonate ion-exchange are included, at present using reverse osmosis membrane
And the way of distillation is the main flow in market.
Though Chinese desalinization possesses industrialized development condition substantially, economy is to determine that its is wide variety of important
Factor.At home, " cost and investment cost are too high, and energy resource consumption is serious ", it is always treated as being that desalinization is difficult to courageously make
Subject matter.
Utility model content
Main purpose of the present utility model is to provide a kind of clean energy resource desalinization and salt making system, existing to solve
The problem of desalinization cost is too high in technology, energy resource consumption is serious.
To achieve these goals, according to one side of the present utility model, there is provided a kind of clean energy resource desalinization
And salt making system, it includes：Clean energy resource generator unit；Electro-desalting unit, electro-desalting unit and clean energy resource generator unit electricity
Connection；Reverse osmosis unit, the seawer outlet pipeline of electro-desalting unit are connected with the sea intake pipeline of reverse osmosis unit；And system
Salt unit, the concentrated water of the concentrated water inlet pipeline of salt manufacturing unit the concentrated water outlet conduit with electro-desalting unit, reverse osmosis unit respectively
Outlet conduit is connected.
Further, electro-desalting unit be arranged in parallel it is multiple.
Further, electro-desalting unit includes：Desalter, the seawer outlet pipeline of desalter and the seawater of reverse osmosis unit
Inlet pipeline is connected；Fairing, fairing electrically connect with desalter, and clean energy resource generator unit is electrically connected with fairing
Connect.
Further, system also includes anti-cleaning unit, the inlet channel of anti-cleaning unit and the fresh water of reverse osmosis unit
Outlet conduit is connected, the outlet conduit of anti-cleaning unit respectively with anti-the rinse water inlet pipeline and reverse osmosis unit of desalter
Anti- rinse water inlet pipeline is connected.
Further, desalter is provided with anode electrode and cathode electrode, and fairing is provided with positive electrode and negative electrode；
When electro-desalting unit is in desalination state, anode electrode is connected with positive electrode, and cathode electrode is connected with negative electrode；Work as electro-desalting
When unit is in anti-cleaning state, anode electrode is connected with negative electrode, and cathode electrode is connected with positive electrode.
Further, anti-cleaning unit includes：Water storing tank, the inlet channel of water storing tank and the water outlet of reverse osmosis unit
Pipeline is connected；Electro-desalting cleaning pump, the inlet channel of electro-desalting cleaning pump are connected with the outlet conduit of water storing tank, electro-desalting cleaning
The outlet conduit of pump is connected with the anti-rinse water inlet pipeline of desalter；Counter-infiltration cleaning pump, the water inlet pipe of counter-infiltration cleaning pump
Road is connected with the outlet conduit of water storing tank, the outlet conduit of counter-infiltration cleaning pump and the anti-rinse water inlet pipeline of reverse osmosis unit
It is connected.
Further, clean energy resource generator unit is wind-power generation unit, solar energy heating generator unit or photovoltaic hair
Electric unit.
Further, system also includes：Sedimentation basin；Filter, seawer outlet pipeline and the electro-desalting list of filter
The sea intake pipeline of member is connected, and the sea intake pipeline of filter is connected with the seawer outlet pipeline of sedimentation basin.
Further, salt manufacturing unit includes：Collecting tank, the concentrated water inlet pipeline of collecting tank are dense with electro-desalting unit respectively
Water exit conduit, the concentrated water outlet conduit of reverse osmosis unit are connected；Evaporation element, the concentrated water inlet pipeline of evaporation element is with collecting
The concentrated water outlet conduit of tank is connected；Drying device, the inlet pipeline of drying device are connected with the salt slurry outlet conduit of evaporation element；
And solar energy heating unit, solar energy heating unit are used to provide heat to evaporation element.
Further, solar energy heating unit includes：Heat-transfer Oil Pump, the inflow pipeline of Heat-transfer Oil Pump and going out for evaporation element
Oil-piping is connected；Slot type heat collecting field, the inflow pipeline of slot type heat collecting field are connected with the flowline of Heat-transfer Oil Pump, slot type heat collecting field
Flowline be connected with the inflow pipeline of evaporation element.
Using the technical solution of the utility model, there is provided a kind of clean energy resource desalinization and salt making system.The system
Including clean energy resource generator unit, electro-desalting unit, reverse osmosis unit and salt manufacturing unit, electro-desalting unit is sent out with clean energy resource
Electric unit electrically connects；The seawer outlet pipeline of electro-desalting unit is connected with the sea intake pipeline of reverse osmosis unit；Salt manufacturing unit
Concentrated water inlet pipeline the concentrated water outlet conduit with electro-desalting unit, the concentrated water outlet conduit of reverse osmosis unit are connected respectively.
Above-mentioned clean energy resource desalinization and salt making system, it can be supplied using clean energy resource generator unit to electro-desalting unit
Electricity, the electrochemical desalting of electro-desalting unit is combined with the membrane separation technique of reverse osmosis unit, is a kind of sustainable development
Desalination technology, on the basis of efficiently desalinizing seawater, it can effectively solve the problem that the energy resource consumption in desalting process is high, dense
The problem of brine discharge and too high cost of investment.Meanwhile the concentrated water separated can also be handled using salt manufacturing unit,
Nacl is prepared, has further reclaimed the salts resources in seawater.
Brief description of the drawings
The Figure of description for forming the part of the application is used for providing further understanding to of the present utility model, this practicality
New schematic description and description is used to explain the utility model, does not form to improper restriction of the present utility model.
In the accompanying drawings：
Fig. 1 is shown according to a kind of clean energy resource desalinization of embodiment of the present utility model and salt making system signal
Figure.
Wherein, above-mentioned accompanying drawing marks including the following drawings：
10th, clean energy resource generator unit；20th, electro-desalting unit；21st, desalter；22nd, fairing；30th, counter-infiltration fills
Put；40th, salt manufacturing unit；41st, collecting tank；42nd, evaporation element；43rd, drying device；44th, solar energy heating unit；441st, conduction oil
Pump；442nd, slot type heat collecting field；50th, anti-cleaning unit；51st, water storing tank；52nd, electro-desalting cleaning pump；53rd, counter-infiltration cleaning pump；60、
Sedimentation basin；70th, filter.
Embodiment
It should be noted that in the case where not conflicting, the feature in embodiment and embodiment in the application can phase
Mutually combination.Describe the utility model in detail below with reference to the accompanying drawings and in conjunction with the embodiments.
The application is described in further detail below in conjunction with specific embodiment, these embodiments are it is not intended that limit this
Apply for scope claimed.
As described by background section, desalinization cost of the prior art is too high, energy resource consumption is serious.
In order to solve this problem, the utility model provides a kind of clean energy resource desalinization and salt making system, such as Fig. 1
Shown, it includes：Clean energy resource generator unit 10, electro-desalting unit 20, reverse osmosis unit 30 and salt manufacturing unit 40, electro-desalting
Unit 20 electrically connects with clean energy resource generator unit 10；The seawer outlet pipeline of electro-desalting unit 20 and the sea of reverse osmosis unit 30
Water inlet pipeline is connected；The concentrated water inlet pipeline of salt manufacturing unit 40 concentrated water outlet conduit, the reverse osmosis with electro-desalting unit 20 respectively
The concentrated water outlet conduit of saturating device 30 is connected.
In the operating process of reality, seawater enters electro-desalting unit 20 by pipeline, and electro-desalting unit 20 passes through cleaning
Energy generator unit 10 obtains electric energy.Seawater enters when being flowed after electro-desalting unit 20 between yin, yang electrode by electric field force
Effect, charged particle by electrode adsorption and is stored in electric double layer respectively to the electrode transfer of oppositely charged in water.Pass through
Electrode surface enrichment concentration, finally realizes the separation of salt and water in seawater.The seawater for completing electrochemical desalting fills into counter-infiltration
Put 30, hydrone constantly passes through film, flows into central tube by producing water flow passage, then the impurity in outflow water at one end, such as from
Son, organic matter, bacterium, virus etc., the influent side of film is trapped within, is then flowed out in concentrated water water side, so as to reach seawater depth
Isolation of purified purpose is spent, desalination rate can reach 99.8%.Water after qualified can be through pipeline to city fresh water pipe network.System
The concentrated water that electro-desalting unit 20 and reverse osmosis unit 30 come out can be carried out dehydration salt manufacturing by salt unit 40, further to reclaim sea
Salts resources in water.
Above-mentioned clean energy resource desalinization and salt making system, it can be supplied using clean energy resource generator unit to electro-desalting unit
Electricity, the electrochemical desalting of electro-desalting unit is combined with the membrane separation technique of reverse osmosis unit, is a kind of sustainable development
Desalination technology, on the basis of efficiently desalinizing seawater, it can effectively solve the problem that the energy resource consumption in desalting process is high, dense
The problem of brine discharge and too high cost of investment.
In a kind of preferred embodiment, as shown in figure 1, electro-desalting unit 20 includes desalter 21 and fairing 22,
The seawer outlet pipeline of desalter 21 is connected with the sea intake pipeline of reverse osmosis unit 30；Fairing 22 and the electricity of desalter 21
Connection, clean energy resource generator unit 10 electrically connect with fairing 22.Fairing 22 can be by clean energy resource generator unit 10
Caused alternating current Transformer Rectifier is that direct current is supplied to desalter 21, and electricity is completed under electric field action of the seawater in desalter 21
Chemical decladding.
In a kind of preferred embodiment, as shown in figure 1, system also includes anti-cleaning unit 50, anti-cleaning unit 50
Inlet channel is connected with the fresh water outlet pipe of reverse osmosis unit 30, the outlet conduit of anti-cleaning unit 50 respectively with desalter 21
Anti- rinse water inlet pipeline, the anti-rinse water inlet pipeline of reverse osmosis unit 30 is connected.Desalination in electro-desalting unit 20
When the electrode of tank 21 reaches adsorption saturation, anti-cleaning and regeneration can be carried out to desalter 21 using anti-cleaning unit 50 and be allowed to recover
Effect.When reverse osmosis unit 30 is contaminated, and effluent index can not meet to require, anti-cleaning unit 50 can also be utilized to it
Cleaning is carried out to be allowed to recover effect.
In a kind of preferred embodiment, desalter 21 is provided with anode electrode and cathode electrode, and fairing 22 is set
There are positive electrode and negative electrode；When electro-desalting unit 20 is in desalination state, anode electrode is connected with positive electrode, cathode electrode with
Negative electrode is connected；When electro-desalting unit 20 is in anti-cleaning state, anode electrode is connected with negative electrode, cathode electrode and positive electricity
Extremely it is connected.So, when electro-desalting unit 20 reaches saturation, quickly by positive and negative electrode moment reversal connection, enrichment is at the electrode surface
Charged particle (or ion) anti-cleaning current or electric field force in the presence of, be shed to the bottom of desalter 21 from electrode surface,
Even if by electrode regeneration.
Preferably, cathode assembly and anode assemblies be set respectively in desalter 21, and cathode assembly and anode assemblies can be by
Conductive flat board (cylinder) material is made, and is arranged on using horizontal (either vertical) mode on insulating support (or suspension bracket), cloudy
Distance is according to Seawater Treatment amount size, spacing reasonable in design between pole component and anode assemblies.Fairing 22 exports direct current
Electricity, positive pole connect on the anode electrode, and negative pole connects on the cathode electrode.Seawater enters from one end of desalter 21 and is separated by by two electrodes
The space formed, flowed out from the other end.
In a kind of preferred embodiment, electro-desalting unit 20 is multiple to be arranged in parallel.So, multiple electro-desalting units
20 alternately can regenerate in desalination, can ensure the continuity of desalination, while can also improve the treating capacity of seawater.With two
Exemplified by electro-desalting unit 20：
It is that 1# electro-desalting unit 20 brings into operation first, alternating current Transformer Rectifier is direct current by fairing 22, is applied
Electrostatic field is formed on the cathode electrode and anode electrode being added in desalter 22.By electricity when seawater flows between yin, yang electrode
The effect of field force, charged particle by electrode adsorption and is stored in electric double layer respectively to the electrode transfer of oppositely charged in water,
Until Electro Sorb process terminates when electrode reaches saturation.Now, 2# electro-desalting unit 20 is brought into operation, and 1# electro-desalting units are opened
Begin to regenerate.1# electro-desalting units remove dc source, and positive and negative electrode moment reversal connection are enriched on yin, yang electrode surface
Charged particle (or ion) anti-cleaning current or electric field force in the presence of, be shed to the bottom of desalter 21 from electrode surface,
Electrode regeneration process terminates.Two alternately operatings of electro-desalting unit 20 carry out Electro Sorb and regeneration, are enriched with by electrode surface dense
Contracting, finally realizes the separation of salt and water, desalination rate can reach 70%.
In a kind of preferred embodiment, as shown in figure 1, anti-cleaning unit 50 includes water storing tank 51, electro-desalting cleaning pump
52 and counter-infiltration cleaning pump 53, the inlet channel of water storing tank 51 be connected with the fresh water outlet pipe of reverse osmosis unit 30；Electricity is de-
The inlet channel of salt cleaning pump 52 is connected with the outlet conduit of water storing tank 51, the outlet conduit and desalter of electro-desalting cleaning pump 52
21 anti-rinse water inlet pipeline is connected；The inlet channel of counter-infiltration cleaning pump 53 is connected with the outlet conduit of water storing tank 51, instead
The outlet conduit of infiltration cleaning pump 53 is connected with the anti-rinse water inlet pipeline of reverse osmosis unit 30.So, device can be utilized
Fresh water after is handled itself is regenerated to electro-desalting unit 20, and cleaning reverse osmosis unit 30 is cleaned.
In a kind of preferred embodiment, clean energy resource generator unit 10 is wind-power generation unit, solar energy heating generating
Unit or photovoltaic generation unit.What this several generator unit relied on is wind energy, clean energy resource as solar energy, can enter one
Step reduces cost and the energy resource consumption of desalinization.
Preferably, wind power generation is made up of head, swivel, empennage, blade.The operation principle is to drive wind using wind-force
Propeller Blade piece rotates, then lifts the speed of rotation through booster engine, to promote electrical power generators.
Preferably, solar energy heating generates electricity and is made up of collecting system, Heat transmission and exchange system, electricity generation system.The work
It is the steam that the heat energy absorbed is converted into working medium by solar thermal collector as principle, then driving steam turbine generates electricity.
Preferably, photovoltaic generation is made up of solar panel (component), controller and inverter three parts.The work
It is that solar radiant energy is directly changed into electric energy as principle, the basic device of light-electricity conversion is exactly solar cell.Solar energy
Battery carries out packaging protection after series connection can form the solar module of large area, then coordinate the parts such as power controller i.e.
Form photovoltaic power generation apparatus.
In a kind of preferred embodiment, as shown in figure 1, system also includes sedimentation basin 60 and filter 70, filtering dress
70 seawer outlet pipeline is put with the sea intake pipeline of electro-desalting unit 20 to be connected, the sea intake pipeline of filter 70 with
The seawer outlet pipeline of sedimentation basin 60 is connected.Seawater enters sedimentation basin 60, can utilize gravitational settling effect by density ratio seawater
Big suspended particulate removes from seawater.Filter 70 is gone successively to, small suspension in seawater can be removed or colloidal state is miscellaneous
Matter.The seawater for completing filtering enters the progress desalting of electro-desalting unit 20.
In a kind of preferred embodiment, as shown in figure 1, salt manufacturing unit 40 includes collecting tank 41, evaporation element 42, dry
Device 43 and solar energy heating unit 44, the concentrated water inlet pipeline concentrated water outlet with electro-desalting unit 20 respectively of collecting tank 41
Pipeline, the concentrated water outlet conduit of reverse osmosis unit 30 are connected；The concentrated water inlet pipeline of evaporation element 42 and the concentrated water of collecting tank 41
Outlet conduit is connected；The inlet pipeline of drying device 43 is connected with the salt slurry outlet conduit of evaporation element 42；Solar energy heating list
Member 44 is used to provide heat to evaporation element 42.Produced in the regenerative process of electro-desalting unit 20 and the cleaning process of reverse osmosis unit 30
- salt concentrated water (bittern) be collected storage into collecting tank 41, enter back into evaporation element 42 by-salt concentrated water (bittern) carry out
It is concentrated by evaporation.The salt slurry of crystallization generation, which enters in drying device 43, to be dried, and drying device 43 is sent into preferably by air blower
Hot-air carry out fluidized drying, dry salt goes storehouse to transport outward by belt conveyor.Can using solar energy heating unit 44
Heat is provided to evaporation element 42, to accelerate evaporation process.
In a kind of preferred embodiment, as shown in figure 1, solar energy heating unit 44 includes Heat-transfer Oil Pump 441 and slot type
Heat collecting field 442, the inflow pipeline of Heat-transfer Oil Pump 441 are connected with the flowline of evaporation element 42；The oil-feed of slot type heat collecting field 442
Pipeline is connected with the flowline of Heat-transfer Oil Pump 441, the flowline of slot type heat collecting field 442 and the inflow pipeline of evaporation element 42
It is connected.So, closed conduction oil loop heating system is formed, solar energy collecting can be got up using slot type heat collecting field 442,
Heat conduction oil and provide heat to evaporation element 42 as heat transfer medium.
Preferably, slewing equipment is controlled by sun tracking system, drives slot type heat collecting field 442 to rotate, timely solar tracking, make the sun
To on condenser minute surface, condenser reflexes to the light from the sun on thermal-collecting tube light direct beam, the conduction oil in heating tube, passes through
Heat-transfer Oil Pump 441, which circulates, brings heat energy into evaporation element 42.It is highly preferred that the inflow pipeline of Heat-transfer Oil Pump 441 also fills with drying
Put 43 flowline to be connected, the flowline of slot type heat collecting field 442 is connected with the inflow pipeline of drying device 43, so can be with
Heat is provided for drying device 43.It is further preferred that solar energy heating unit 44 also includes heat storage can, to by unnecessary heat
It can store, sustainable heat energy is provided for night.
As can be seen from the above description, the utility model the above embodiments realize following technique effect：This reality
With the clean energy resource desalinization of new offer and salt making system, can be supplied using clean energy resource generator unit to electro-desalting unit
Electricity, the electrochemical desalting of electro-desalting unit is combined with the membrane separation technique of reverse osmosis unit, is a kind of sustainable development
Desalination technology, on the basis of efficiently desalinizing seawater, it can effectively solve the problem that the energy resource consumption in desalting process is high, dense
The problem of brine discharge and too high cost of investment.
Preferred embodiment of the present utility model is the foregoing is only, is not limited to the utility model, for this
For the technical staff in field, the utility model can have various modifications and variations.It is all in the spirit and principles of the utility model
Within, any modification, equivalent substitution and improvements made etc., it should be included within the scope of protection of the utility model.
Claims (10)
1. a kind of clean energy resource desalinization and salt making system, it is characterised in that including：
Clean energy resource generator unit (10)；
Electro-desalting unit (20), the electro-desalting unit (20) electrically connect with the clean energy resource generator unit (10)；
Reverse osmosis unit (30), the seawer outlet pipeline of the electro-desalting unit (20) and the seawater of the reverse osmosis unit (30)
Inlet pipeline is connected；And
Salt manufacturing unit (40), the concentrated water inlet pipeline of the salt manufacturing unit (40) concentrated water with the electro-desalting unit (20) respectively
Outlet conduit, the concentrated water outlet conduit of the reverse osmosis unit (30) are connected.
2. clean energy resource desalinization according to claim 1 and salt making system, it is characterised in that the electro-desalting unit
(20) it is multiple to be arranged in parallel.
3. clean energy resource desalinization according to claim 1 or 2 and salt making system, it is characterised in that the electro-desalting
Unit (20) includes：
Desalter (21), the seawer outlet pipeline of the desalter (21) and the sea intake pipeline of the reverse osmosis unit (30)
It is connected；
Fairing (22), the fairing (22) electrically connect with the desalter (21), the clean energy resource generator unit
(10) electrically connected with the fairing (22).
4. clean energy resource desalinization according to claim 3 and salt making system, it is characterised in that the system also includes
Anti- cleaning unit (50), the inlet channel of the anti-cleaning unit (50) and the fresh water outlet pipe of the reverse osmosis unit (30)
Be connected, the outlet conduit of the anti-cleaning unit (50) respectively with the anti-rinse water inlet pipeline of the desalter (21) and described
The anti-rinse water inlet pipeline of reverse osmosis unit (30) is connected.
5. clean energy resource desalinization according to claim 4 and salt making system, it is characterised in that the desalter (21)
Anode electrode and cathode electrode are provided with, the fairing (22) is provided with positive electrode and negative electrode；
When the electro-desalting unit (20) is in desalination state, the anode electrode is connected with the positive electrode, the negative electrode
Electrode is connected with the negative electrode；
When the electro-desalting unit (20) is in anti-cleaning state, the anode electrode is connected with the negative electrode, described the moon
Pole electrode is connected with the positive electrode.
6. clean energy resource desalinization according to claim 4 and salt making system, it is characterised in that the anti-cleaning unit
(50) include：
Water storing tank (51), the fresh water outlet pipe phase of the inlet channel and the reverse osmosis unit (30) of the water storing tank (51)
Even；
Electro-desalting cleaning pump (52), the inlet channel of the electro-desalting cleaning pump (52) and the outlet conduit of the water storing tank (51)
It is connected, the outlet conduit of the electro-desalting cleaning pump (52) is connected with the anti-rinse water inlet pipeline of the desalter (21)；
Counter-infiltration cleaning pump (53), the inlet channel of the counter-infiltration cleaning pump (53) and the outlet conduit of the water storing tank (51)
It is connected, the outlet conduit of the counter-infiltration cleaning pump (53) and the anti-rinse water inlet pipeline phase of the reverse osmosis unit (30)
Even.
7. clean energy resource desalinization according to claim 1 or 2 and salt making system, it is characterised in that the cleaning energy
Source generator unit (10) is wind-power generation unit, solar energy heating generator unit or photovoltaic generation unit.
8. clean energy resource desalinization according to claim 1 or 2 and salt making system, it is characterised in that the system is also
Including：
Sedimentation basin (60)；
Filter (70), the seawer outlet pipeline of the filter (70) and the sea intake of the electro-desalting unit (20)
Pipeline is connected, and the sea intake pipeline of the filter (70) is connected with the seawer outlet pipeline of the sedimentation basin (60).
9. clean energy resource desalinization according to claim 1 or 2 and salt making system, it is characterised in that the salt manufacturing list
First (40) include：
Collecting tank (41), the concentrated water inlet pipeline concentrated water outlet with the electro-desalting unit (20) respectively of the collecting tank (41)
Pipeline, the concentrated water outlet conduit of the reverse osmosis unit (30) are connected；
Evaporation element (42), the concentrated water inlet pipeline of the evaporation element (42) and the concentrated water outlet conduit of the collecting tank (41)
It is connected；
Drying device (43), the inlet pipeline of the drying device (43) and the salt slurry outlet conduit phase of the evaporation element (42)
Even；And
Solar energy heating unit (44), the solar energy heating unit (44) are used to provide heat to the evaporation element (42).
10. clean energy resource desalinization according to claim 9 and salt making system, it is characterised in that the solar energy collection
Hot cell (44) includes：
Heat-transfer Oil Pump (441), the flowline phase of the inflow pipeline and the evaporation element (42) of the Heat-transfer Oil Pump (441)
Even；
Slot type heat collecting field (442), the inflow pipeline of the slot type heat collecting field (442) and the flowline of the Heat-transfer Oil Pump (441)
Road is connected, and the flowline of the slot type heat collecting field (442) is connected with the inflow pipeline of the evaporation element (42).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720125517.2U CN206705876U (en) | 2017-02-10 | 2017-02-10 | Clean energy resource desalinization and salt making system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720125517.2U CN206705876U (en) | 2017-02-10 | 2017-02-10 | Clean energy resource desalinization and salt making system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206705876U true CN206705876U (en) | 2017-12-05 |
Family
ID=60472921
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720125517.2U Active CN206705876U (en) | 2017-02-10 | 2017-02-10 | Clean energy resource desalinization and salt making system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206705876U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106630359A (en) * | 2017-02-10 | 2017-05-10 | 碧海舟（北京）节能环保装备有限公司 | Clean energy seawater desalination and salt making system |
| CN110207447A (en) * | 2019-05-29 | 2019-09-06 | 常州大学 | A kind of cooling water treatment system of anti-seawater cooling tower fouling |
-
2017
- 2017-02-10 CN CN201720125517.2U patent/CN206705876U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106630359A (en) * | 2017-02-10 | 2017-05-10 | 碧海舟（北京）节能环保装备有限公司 | Clean energy seawater desalination and salt making system |
| CN110207447A (en) * | 2019-05-29 | 2019-09-06 | 常州大学 | A kind of cooling water treatment system of anti-seawater cooling tower fouling |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106630359A (en) | Clean energy seawater desalination and salt making system | |
| CN105152252B (en) | Comprehensively utilize zero energy consumption sea water desalinating unit of solar energy | |
| Al-Karaghouli et al. | Energy consumption and water production cost of conventional and renewable-energy-powered desalination processes | |
| Gorjian et al. | Applications of solar PV systems in desalination technologies | |
| Al-Karaghouli et al. | Renewable energy opportunities in water desalination | |
| WO2014181898A1 (en) | Large-capacity electric power storage system using thermal energy/chemical potential | |
| Gude et al. | Energy efficiency and renewable energy utilization in desalination systems | |
| CN111003742A (en) | Seawater desalination system for solar photovoltaic waste heat-joule heat gradient utilization | |
| CN106830227A (en) | The membrane capacitance deionizer and processing method of a kind of circular treatment | |
| Kariman et al. | Small scale desalination technologies: A comprehensive review | |
| CN101337749A (en) | Solar desalination process and integrated equipment | |
| CN204674788U (en) | Offshore floating type water-electricity cogeneration platform | |
| CN113039008A (en) | System and method for simultaneous power generation and fresh water generation by membrane distillation | |
| Albloushi et al. | Renewable energy-powered membrane systems for water desalination | |
| CN107522307A (en) | A kind of Oversea wind fresh-water generator and its application process | |
| CN206705876U (en) | Clean energy resource desalinization and salt making system | |
| Kargari et al. | Water desalination: Solar-assisted membrane distillation | |
| CN111268844A (en) | Saline-alkali water desalination circulation system based on micro-grid power supply and application | |
| CN107619079A (en) | A kind of solar energy purification system and its process for purifying water | |
| CN203781962U (en) | Household solar-powered seawater desalination system | |
| CN107416931A (en) | Flexible adapted local cosine transform solar seawater desalination system and method for desalting seawater | |
| Sun et al. | Research progress on the integration and optimal design of desalination process | |
| CN105174576A (en) | Novel seawater desalination system | |
| CN111018023B (en) | Solar desalination water system based on carbon composite hollow fiber membrane and method thereof | |
| El Aimani | Modeling of reverse osmosis water desalination powered by photovoltaic solar energy |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |