CN110272080A - It is a kind of using solar energy and the salt water desalination system of wind energy - Google Patents
It is a kind of using solar energy and the salt water desalination system of wind energy Download PDFInfo
- Publication number
- CN110272080A CN110272080A CN201910568662.1A CN201910568662A CN110272080A CN 110272080 A CN110272080 A CN 110272080A CN 201910568662 A CN201910568662 A CN 201910568662A CN 110272080 A CN110272080 A CN 110272080A
- Authority
- CN
- China
- Prior art keywords
- salt water
- water
- energy
- wind
- solar
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 202
- 150000003839 salts Chemical class 0.000 title claims abstract description 131
- 238000010612 desalination reaction Methods 0.000 title claims abstract description 31
- 238000009833 condensation Methods 0.000 claims description 44
- 230000005494 condensation Effects 0.000 claims description 44
- 238000009834 vaporization Methods 0.000 claims description 34
- 230000008016 vaporization Effects 0.000 claims description 34
- 238000001514 detection method Methods 0.000 claims description 18
- 238000001816 cooling Methods 0.000 claims description 16
- 239000013505 freshwater Substances 0.000 claims description 16
- 239000007788 liquid Substances 0.000 claims description 16
- 238000005286 illumination Methods 0.000 claims description 9
- 238000001704 evaporation Methods 0.000 claims description 5
- 230000005611 electricity Effects 0.000 abstract description 9
- 230000005855 radiation Effects 0.000 abstract description 5
- 238000004821 distillation Methods 0.000 description 12
- 238000000034 method Methods 0.000 description 8
- 239000000567 combustion gas Substances 0.000 description 5
- 239000000295 fuel oil Substances 0.000 description 5
- 238000010248 power generation Methods 0.000 description 4
- 239000003245 coal Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000004134 energy conservation Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- -1 coal-fired Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000001066 destructive effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000003643 water by type Substances 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
- C02F1/008—Control or steering systems not provided for elsewhere in subclass C02F
-
- 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
-
- 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
-
- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J7/00—Circuit arrangements for charging or depolarising batteries or for supplying loads from batteries
- H02J7/34—Parallel operation in networks using both storage and other dc sources, e.g. providing buffering
- H02J7/35—Parallel operation in networks using both storage and other dc sources, e.g. providing buffering with light sensitive cells
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/009—Apparatus with independent power supply, e.g. solar cells, windpower, fuel cells
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/005—Processes using a programmable logic controller [PLC]
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/02—Temperature
-
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/138—Water desalination using renewable energy
- Y02A20/141—Wind power
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/138—Water desalination using renewable energy
- Y02A20/142—Solar thermal; Photovoltaics
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/70—Wind energy
- Y02E10/76—Power conversion electric or electronic aspects
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Power Engineering (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Wind Motors (AREA)
Abstract
The invention discloses a kind of using solar energy and the salt water desalination system of wind energy, including solar power system, wind generator system, battery group and salt water Distallation systm；The solar power system and the wind generator system are connected with the battery group respectively and charge to it；The battery group supplies the salt water Distallation systm electric energy.The present invention utilizes solar energy and wind-power electricity generation, and the radiation energy of solar energy can be converted into thermal energy, can independent operation, do not need input thermal energy and electric energy.It is of the invention it is small in size be easily installed, convenient for being used in the place that spitkit, island etc. are detached from land resources.
Description
Technical field
It is the present invention relates to a kind of salt water desalination system, in particular to a kind of using solar energy and the salt water desalination system of wind energy
System.
Background technique
There are two types of different methods for salt water desalination, and one is the way of distillation, another kind is hyperfiltration.It is needed again in thermal energy abundance
The occasion of sea water desalination is wanted generally to use the way of distillation.Desalination speed is fast, under the occasion not high to the fresh water quality requirements after desalination
Hyperfiltration is generally used, hyperfiltration needs electric energy.Both salt water desalinations need electric energy or thermal energy, general use fire coal,
The modes such as combustion gas or fuel oil provide thermal energy, and electric energy is generally using the electric energy produced by modes such as coal-fired, combustion gas or fuel oils.Currently,
In some islands and some depopulated zones, the supply of fresh water and salt is needed, but power supply system network is generally difficult to cover these ground
Area, and the materials such as coal-fired, combustion gas or fuel oil due to transportation cost it is too high, and be rarely employed；So these areas had both lacked combustion
Coal, combustion gas or fuel oil also lack electric energy, and existing salt water desalination system energy consumption is higher, need to rely on existing electric energy and fire coal,
The thermal energy of the generations such as combustion gas or fuel oil can not voluntarily realize salt water desalination, need from other regional transport fresh waters and salt, and transport
Fresh water and salt cost are also very high.
Summary of the invention
The present invention be solve technical problem present in well-known technique and provide a kind of energy conservation and environmental protection, low cost utilization too
The salt water desalination system of positive energy and wind energy.
The technical scheme adopted by the present invention to solve the technical problems existing in the known art is that a kind of utilize solar energy
And the salt water desalination system of wind energy, including solar power system, wind generator system, battery group and salt water distillation system
System；The solar power system and the wind generator system are connected with the battery group respectively and charge to it；It is described
Battery group supplies the salt water Distallation systm electric energy.
Further, the salt water Distallation systm includes solar thermal collector, vaporization chamber, condensation chamber and the first water pump；
The solar thermal collector, which absorbs the radiation energy of the sun and is converted to thermal energy, to be exported to the vaporization chamber；The vaporization chamber, packet
Salt water input port and salt water delivery outlet are included, the thermal energy from the solar thermal collector is absorbed to heat salt water, exports water
Steam is to the condensation chamber；Water vapour is cooled to liquid fresh water and collected by the condensation chamber；The water outlet of first water pump
Salt water is exported to the salt water input port of the vaporization chamber；The salt water delivery outlet of the vaporization chamber exports the salt water not being evaporated.
Further, the water outlet of first water pump is connected to the cooling working medium input port of the condensation chamber.
Further, the salt water Distallation systm further includes electric heater；The water outlet of first water pump passes through valve
It is connected to the inlet of the electric heater, the liquid outlet of the electric heater is connected to the salt water input port of the vaporization chamber.
Further, the water outlet of first water pump is connected to the cooling working medium input port of the condensation chamber；The electricity
The inlet of heater is connected to by valve with the cooling working medium delivery outlet of the condensation chamber.
Further, the salt water Distallation systm further includes jet pump；The jet pump includes high-pressure mouth, suction inlet and row
Outlet；The high-pressure mouth of the jet pump is connected to by valve with the water outlet of first water pump；The suction inlet of the jet pump
It is connected to respectively with the salt water delivery outlet of the vapor cavity of the condensation chamber and the vaporization chamber.
Further, the suction inlet of the jet pump is connected to by air admission valve with the condensation chamber inner cavity.
Further, the salt water Distallation systm further includes the second water pump；The water inlet of second water pump with it is described cold
The fresh water liquid outlet connection of solidifying room.
It further, further include control system；The control system respectively with the solar power system, the wind-force
Electricity generation system, the battery group and the salt water Distallation systm are connected.
It further, further include detection system, the detection system includes temperature sensor, air velocity transducer and illumination
Sensor is spent, the temperature sensor detects the salt water temperature in the salt water Distallation systm；The air velocity transducer detection is outer
Portion's ambient wind velocity；The illuminance sensor detects the sunlight intensity of illumination；The control system input comes from the inspection
The signal of examining system, output signal control the solar power system, the wind generator system and salt water distillation
The work of system.
The advantages and positive effects of the present invention are: the present invention utilizes solar energy and wind-power electricity generation, and can be by solar energy
Radiation energy be converted into thermal energy, can independent operation, do not need input thermal energy and electric energy.
Existing salt water distillation desalination system enlargement is more, minimizes fewer；It is of the invention it is small in size be easily installed, just
It is used in the place that spitkit, island etc. are detached from land resources.
Existing salt water desalination system needs replacing filter membrane, and maintenance cost is high；Vulnerable part of the present invention is less, only needs periodic cleaning
, maintenance cost is low.
Existing small reverse osmosis desalination system salt concentration is higher, and the present invention is way of distillation desalination, and salt concentration is relatively low.
Detailed description of the invention
Fig. 1 is structural schematic diagram of the invention.
In figure: 1, wind generator system；2, solar power system；3, control system；4, battery group；5, the second valve
Door；6, condensation chamber；7, air admission valve；8, the second pump motor；9, the second water pump；10, third valve；11, the row of jet pump
Outlet；12, jet pump；13, electric heater；14, thermometer；15, vaporization chamber；16, the first valve；17, the first pump motor；
18, the first water pump；19, filter；20, the input port of filter.
Specific embodiment
In order to further understand the content, features and effects of the present invention, hereby enumerating following embodiment, and cooperate attached drawing
Detailed description are as follows:
Referring to Figure 1, a kind of using solar energy and the salt water desalination system of wind energy, including solar power system 2, wind-force
Electricity generation system 1, battery group 4 and salt water Distallation systm；The solar power system 2 and the wind generator system 1 divide
It is not connected with the battery group 4 and charges to it；The battery group 4 supplies the salt water Distallation systm electric energy.It is real in figure
Line indicates that connecting line, dotted line represent electrical connection circuit.
Solar power system 2 is used to for solar radiant energy being transformed into electric energy, and wind generator system 1 is for changing wind energy
At electric energy.Salt water Distallation systm is used to salt water generating fresh water by the way of distillation；Battery group 4 is for storing electric energy, and to salty
Water distillation system etc. exports electric energy.
Wind powered generator system in the prior art can be used in wind generator system 1；Solar power system 2 can be used existing
There is the solar power system 2 in technology.
Preferably, the salt water Distallation systm may include solar thermal collector, vaporization chamber 15, condensation chamber 6 and the first water
Pump 18；The solar thermal collector can absorb the radiation energy of the sun and is converted to thermal energy and exports to the vaporization chamber 15；The steaming
Room 15 is sent out, may include salt water input port and salt water delivery outlet, can absorb the thermal energy from the solar thermal collector to add
Hot salt water, exportable water vapour to the condensation chamber 6；Water vapour can be cooled to liquid fresh water and collected by the condensation chamber 6；
The exportable salt water of water outlet of first water pump 18 is to the salt water input port of the vaporization chamber 15；The salt water of the vaporization chamber 15
The exportable salt water not being evaporated of delivery outlet.Filter is connected before first water pump, 18 input port, salt water enters filter input port
20, impurity is filtered out by filter 19,18 water inlet of the first water pump is input to after filtering, salt water is pressurized by the first water pump 18.
4 output voltage of battery group to first pump motor 17, the operating of the first pump motor 17 drives the first water pump
18 work, by salt water from the salt water storage place pressure-increasing unit such as reservoir, for example are delivered to the salt water input port of vaporization chamber 15, salt water
The energy heats generated in vaporization chamber 15 by solar thermal collector generate vapor.Vapor is exported to condensation chamber 6, is being condensed
After being cooled in room 6, becomes liquid water, in the fresh water collecting slot that condensation chamber 6 is pooled to condensation chamber 6, then export.It is not steamed
The salt water of hair is then discharged from the salt water delivery outlet of the vaporization chamber 15.
Preferably, the water outlet of first water pump 18 can be connected to the cooling working medium input port of the condensation chamber 6.In this way
First water pump 18 can both convey distillatory salt water raw material, can also provide coolant liquid to condensation chamber 6, simplify system, subtract
The setting of the cooling working medium pump of few condensation chamber 6.
Preferably, the salt water Distallation systm may also include electric heater 13；The water outlet of first water pump 18 can lead to
It crosses valve to be connected to the inlet of the electric heater 13, the liquid outlet of the electric heater 13 can be salty with the vaporization chamber 15
Water input connection.The water outlet of first water pump 18 can connect the first valve 16, and the output of the first valve 16 can be divided into two
Road, wherein being connected to all the way with the cooling working medium input port of the condensation chamber 6；Another way can pass through valve and the electric heater 13
Inlet connection；For controlling the salt water amount into the vaporization chamber 15.First valve 16 can be shut-off valve, flow control valve
Or flow divider valve；The pattern of first valve 16 can be hand-operated valve or motor-driven valve, and the first valve 16 is available using flow divider valve
In adjusting and distribution two-way output flow.
It is when sunlight illumination deficiency, using the electric energy stored in battery group 4, to distillation using electric heater 13
Salt water raw material is preheated.Function and the application of system are expanded, is easy to use.The water outlet of first water pump 18
Mouth can be connected to the cooling working medium input port of the condensation chamber 6；The inlet of the electric heater 13 can by valve with it is described
The cooling working medium delivery outlet of condensation chamber 6 is connected to.The lower salt water of temperature that first water pump 18 exports, in condensation chamber 6 and water
Steam heat exchange, from the higher salt water of 6 output temperature of condensation chamber after heat exchange, the higher salt water of temperature is entered by electric heater 13 to be steamed
Send out the salt water input port of room 15, the thermal energy of vapor liquefaction release absorbable in this way；Reduce the use of electric energy, energy conservation and environmental protection.
Preferably, the salt water Distallation systm may also include jet pump 12；The jet pump 12 may include high-pressure mouth, sucking
Mouth and outlet；The high-pressure mouth of the jet pump 12 can be connected to by valve with the water outlet of first water pump 18；The spray
The suction inlet for penetrating pump 12 can be connected to the salt water delivery outlet of the vapor cavity of the condensation chamber 6 and the vaporization chamber 15 respectively.
The salt water waste liquid not being evaporated is discharged in the outlet 11 of the jet pump, can be discharged to the outside reservoir etc..Jet pump 12 can be borrowed
The energy for the fluid for helping the first water pump 18 to export does power source, for aspirating the salt water waste liquid not being evaporated in vaporization chamber 15,
And the air in the condensation chamber 6 and vaporization chamber 15.It extracts the gas in container using the high-speed jet by nozzle
To obtain vacuum, to reduce vapo(u)rizing temperature and improve separative efficiency, the evaporation rate of salt water is improved.
The output of first valve 16 can be divided into two-way, wherein being connected to all the way with the cooling working medium input port of the condensation chamber 6；
Another way is connected to the input port of the second valve 5；The output of second valve 5 can be divided into two-way, wherein all the way with the jet pump
12 high-pressure mouth connection；Another way is connected to the input port of third valve 10, and the delivery outlet of third valve 10 can add with the electricity
The inlet of hot device 13 is connected to；Wherein.Second valve 5 can be shut-off valve, flow control valve or flow divider valve, the second valve 5
Pattern can be hand-operated valve or motor-driven valve；Second valve 5 can be used for adjusting and distributing two-way output flow using flow divider valve.
Third valve 10 can be shut-off valve or flow control valve, and the pattern of third valve 10 can be hand-operated valve or motor-driven valve；Third valve
10 for controlling the salt water amount into the vaporization chamber 15.
The driving method of hand-operated valve is the executing agency of manual actuation valve；The driving method of motor-driven valve is electromagnetic coil drive
Dynamic executing agency.
Preferably, the suction inlet of the jet pump 12 can be connected to by air admission valve 7 with 6 inner cavity of condensation chamber.Very
Empty destructive valve 7 can play the effect of protection system safety.
Preferably, the salt water Distallation systm may also include the second water pump 9；The water inlet of second water pump 9 can be with institute
State the fresh water liquid outlet connection of condensation chamber 6.To avoid liquid in condensation chamber 6 from retaining excessive influence vapor liquefaction efficiency, pass through
Second water pump 9 exports the liquid fresh water collected in condensation chamber 6.4 output voltage of battery group is to the second pump motor 8, and second
The operating of pump motor 8 drives the work of the second water pump 9, and the liquid fresh water that fresh water is collected out of condensation chamber 6 is exported to external water storage
In container.
Preferably, the present invention may also include control system 3；The control system 3 can respectively with the solar power generation system
System 2, the wind generator system 1, the battery group 4 and the salt water Distallation systm are connected.The control system 3 exports
Signal controls the solar power system 2, the wind generator system 1, the battery group 4 and salt water distillation system
The work of system.The control system 3 may include controller, contactor, electrothermal relay, breaker etc., and controller can be compiled for PLC
Existing skill can be selected in range controller, industrial personal computer etc., PLC programmable controller, industrial personal computer, contactor, electrothermal relay, breaker etc.
Product in art.
Further, the present invention may also include detection system, and detection system is used to detect the salt water in salt water Distallation systm
Temperature, external environment wind speed, sunlight intensity of illumination and electric energy of battery group 4 etc.；The detection system may include temperature
Sensor, air velocity transducer and illuminance sensor, the temperature sensor can detect salty in the salt water Distallation systm
Coolant-temperature gage；The air velocity transducer can detect external environment wind speed；The illuminance sensor can detect sunlight intensity of illumination；
The control system 3 inputs the signal from the detection system, and output signal controls the solar power system 2, described
The work of wind generator system 1 and the salt water Distallation systm.
For example, the temperature sensor of detection system can detect salt water temperature in vaporization chamber 15, the input of control system 3 is from temperature
Spend the signal of sensor；If temperature is lower than setting value, 3 output signal of control system makes electric heater 13 work；Detection system
The detectable external environment wind speed of the air velocity transducer of system, control system 3 input the signal from air velocity transducer；If
Wind speed is below or above the working range of wind generator system 1, then 3 output signal of control system stops wind generator system 1
Work；Detection system can detect the electric energy of battery group 4；If the electric energy of battery group 4 is full of, and salt water distillation system
It unites in idle situation, then 3 output signal of control system makes the solar power system 2 and the wind generator system 1
It stops working；If the electric energy of battery group 4 is insufficient, it is lower than setting value, then 3 output signal of control system sends out the solar energy
Electric system 2 and the work power generation of the wind generator system 1；It is strong that the illuminance sensor of detection system can detect sunlight illumination
Degree, control system 3 input the signal from illuminance sensor；If sunlight intensity of illumination is lower than setting value, and battery
The output voltage of group 4 is lower than the operating voltage of salt water Distallation systm, then 3 output signal of control system makes the salt water Distallation systm
It stops working.
Product in the prior art can be selected in the sensors such as temperature sensor, air velocity transducer and illuminance sensor.
By using PLC programmable controller in the prior art, industrial personal computer, contactor, electrothermal relay, breaker, temperature
Spend the electrical components such as sensor, air velocity transducer, illuminance sensor, motor, electromagnetic valve coil and corresponding conventional control electricity
The work of solar power system 2, the wind generator system 1 and the salt water Distallation systm is realized on road.Specific circuit
Connection and control method can be according to product descriptions, using the circuit connection and conventional control methods of conventional technical means.
Illustrate workflow and working principle of the invention below according to a preferred embodiment of the present invention:
It is a kind of using solar energy and the salt water desalination system of wind energy, including solar power system 2, wind generator system 1,
Battery group 4, control system 3, detection system and salt water Distallation systm；Salt water Distallation systm includes the first water pump 18, the sun
It can heat collector, vaporization chamber 15, condensation chamber 6, electric heater 13, jet pump 12, the second water pump 9, air admission valve 7, thermometer 14
And the equal components of filter 19 for filtering salt water impurity.Control system 3 respectively with the solar power system 2, institute
It states wind generator system 1, the battery group 4 and the salt water Distallation systm to be connected, for controlling the solar power generation
The work of system 2, the wind generator system 1, the battery group 4 and the salt water Distallation systm.Detection system can wrap
Temperature sensor, air velocity transducer and illuminance sensor are included, for detecting the salt water temperature in salt water Distallation systm, outside
The electric energy of ambient wind velocity, sunlight intensity of illumination and battery group 4.
Solar power system 2 and wind generator system 1 are produced electricl energy for generating electricity, and solar power system 2 is by the sun
Radiation energy is transformed into electric energy, and wind energy is transformed into electric energy by wind generator system 1.It can be by solar power system 2 and wind-power electricity generation
The electric energy that system 1 generates charges to battery group 4 and electric energy is stored in battery group 4, in case in the item for not having power generation
It is used under part, control system 3 receives the signal for carrying out self-check system, and the voltage of detection system detection battery group 4 reaches regulation
Value and when illuminance meets the requirements, 3 output signal of control system make solar power system 2, wind generator system 1 and salty
Water distillation system work.3 output signal of control system controls the first pump motor 17, the second pump motor 8, electric heater 13 etc.
The operation and stopping of electrical equipment.
Salt water filters out impurity by filter 19, and 18 water inlet of the first water pump is input to after filtering, is increased by the first water pump 18
Salty effect of pressure water, and it is divided into two-way in water outlet, jet pump 12 is passed through with certain speed all the way, extracts condensation chamber 6 and vaporization chamber 15
Interior air makes its vacuum degree up to 85% or more, enters the cooling working medium pipeline of condensation chamber 6, the sendout of specific salt water all the way
It is adjusted by the first valve 16.Need to condense there are no steam when beginning, in the case where there is steam with steam heat-exchanging, steam
It is condensed into fresh water, salt water temperature is raised, and the at this moment starting of electric heater 13 is that salt water preheats in advance, and the temperature of heating is to evaporate
Room 15 is adjusted on the basis of exporting salt water temperature, and subsequently into vaporization chamber 15, at this moment the salt water of vaporization chamber 15 absorbs the sun
The thermal energy for radiating transformation, gradually heats up, starts to evaporate under vacuum conditions, and steam enters condensation chamber 6 and cooling working medium heat exchange,
It is cooling by the lower salt water of temperature as cooling working medium, it is discharged to be liquefied as fresh water by the second water pump 9.Do not have in vaporization chamber 15
There is the salt water being evaporated to be discharged by jet pump 12, the process of entire desalination is completed.
Embodiment described above is merely to illustrate technical idea and feature of the invention, in the art its object is to make
Technical staff it will be appreciated that the contents of the present invention and implement accordingly, patent model of the invention only cannot be limited with the present embodiment
It encloses, i.e., same changes or modifications made by all disclosed spirit are still fallen in the scope of the patents of the invention.
Claims (10)
1. a kind of using solar energy and the salt water desalination system of wind energy, which is characterized in that sent out including solar power system, wind-force
Electric system, battery group and salt water Distallation systm；The solar power system and the wind generator system respectively with institute
Battery group is stated to be connected and charge to it；The battery group supplies the salt water Distallation systm electric energy.
2. according to claim 1 using solar energy and the salt water desalination system of wind energy, which is characterized in that the salt water steams
The system of evaporating includes solar thermal collector, vaporization chamber, condensation chamber and the first water pump；The solar thermal collector absorbs the spoke of the sun
It penetrates and can and be converted to thermal energy and export to the vaporization chamber；The vaporization chamber comprising salt water input port and salt water delivery outlet are inhaled
The thermal energy from the solar thermal collector is received to heat salt water, output water vapour to the condensation chamber；The condensation chamber will
Water vapour is cooled to liquid fresh water and collects；The salt water that the water outlet of first water pump exports salt water to the vaporization chamber inputs
Mouthful；The salt water delivery outlet of the vaporization chamber exports the salt water not being evaporated.
3. according to claim 2 using solar energy and the salt water desalination system of wind energy, which is characterized in that first water
The water outlet of pump is connected to the cooling working medium input port of the condensation chamber.
4. according to claim 2 using solar energy and the salt water desalination system of wind energy, which is characterized in that the salt water steams
The system of evaporating further includes electric heater；The water outlet of first water pump is connected to by valve with the inlet of the electric heater,
The liquid outlet of the electric heater is connected to the salt water input port of the vaporization chamber.
5. according to claim 4 using solar energy and the salt water desalination system of wind energy, which is characterized in that first water
The water outlet of pump is connected to the cooling working medium input port of the condensation chamber；The inlet of the electric heater by valve with it is described
The cooling working medium delivery outlet of condensation chamber is connected to.
6. according to claim 2 using solar energy and the salt water desalination system of wind energy, which is characterized in that the salt water steams
The system of evaporating further includes jet pump；The jet pump includes high-pressure mouth, suction inlet and outlet；The high-pressure mouth of the jet pump passes through
Valve is connected to the water outlet of first water pump；The suction inlet of the jet pump respectively with the vapor cavity of the condensation chamber
And the salt water delivery outlet connection of the vaporization chamber.
7. according to claim 6 using solar energy and the salt water desalination system of wind energy, which is characterized in that the jet pump
Suction inlet be connected to the condensation chamber inner cavity by air admission valve.
8. according to claim 2 using solar energy and the salt water desalination system of wind energy, which is characterized in that the salt water steams
The system of evaporating further includes the second water pump；The water inlet of second water pump is connected to the fresh water liquid outlet of the condensation chamber.
9. according to any one of claims 1 to 8 using solar energy and the salt water desalination system of wind energy, which is characterized in that also
Including control system；The control system respectively with the solar power system, the wind generator system, the battery
Group and the salt water Distallation systm are connected.
10. described utilizing solar energy and the salt water desalination system of wind energy according to claim 9 is any, which is characterized in that also wrap
Detection system is included, the detection system includes temperature sensor, air velocity transducer and illuminance sensor, the temperature sensing
Device detects the salt water temperature in the salt water Distallation systm；The air velocity transducer detects external environment wind speed；The illuminance
Sensor detects the sunlight intensity of illumination；The control system inputs the signal from the detection system, output signal
Control the work of the solar power system, the wind generator system and the salt water Distallation systm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910568662.1A CN110272080A (en) | 2019-06-27 | 2019-06-27 | It is a kind of using solar energy and the salt water desalination system of wind energy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910568662.1A CN110272080A (en) | 2019-06-27 | 2019-06-27 | It is a kind of using solar energy and the salt water desalination system of wind energy |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110272080A true CN110272080A (en) | 2019-09-24 |
Family
ID=67962570
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910568662.1A Pending CN110272080A (en) | 2019-06-27 | 2019-06-27 | It is a kind of using solar energy and the salt water desalination system of wind energy |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110272080A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114249334A (en) * | 2021-12-15 | 2022-03-29 | 唐山市银海食盐有限公司 | Wind, light and electricity complementary system for processing granular sea salt |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102351263A (en) * | 2011-07-14 | 2012-02-15 | 天津大学 | Active solar energy and wind energy coupling seawater desalination plant |
| CN104556278A (en) * | 2015-01-15 | 2015-04-29 | 济南祥丰能源技术有限公司 | Solar energy and wind energy combined passive vacuum sea water desalination device |
| CN106115830A (en) * | 2016-08-05 | 2016-11-16 | 重庆市三耕储节能环保科技有限公司 | A kind of renewable sources of energy sea water automatic processing device |
| WO2017185930A1 (en) * | 2016-04-27 | 2017-11-02 | 武汉凯迪工程技术研究总院有限公司 | Combined solar-powered seawater desalination and air-conditioned cooling method and system having high efficiency |
| CN207212586U (en) * | 2017-07-28 | 2018-04-10 | 海南电网有限责任公司三沙供电局 | It is a kind of to utilize wind energy and the Sea Water Pumped Storage Station ship of solar energy |
| CN209010175U (en) * | 2018-06-01 | 2019-06-21 | 华北电力大学 | A kind of desalination plant cooperateing with solar energy and wind energy |
| CN210620293U (en) * | 2019-06-27 | 2020-05-26 | 中海油能源发展股份有限公司 | Salt water desalination system utilizing solar energy and wind energy |
-
2019
- 2019-06-27 CN CN201910568662.1A patent/CN110272080A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102351263A (en) * | 2011-07-14 | 2012-02-15 | 天津大学 | Active solar energy and wind energy coupling seawater desalination plant |
| CN104556278A (en) * | 2015-01-15 | 2015-04-29 | 济南祥丰能源技术有限公司 | Solar energy and wind energy combined passive vacuum sea water desalination device |
| WO2017185930A1 (en) * | 2016-04-27 | 2017-11-02 | 武汉凯迪工程技术研究总院有限公司 | Combined solar-powered seawater desalination and air-conditioned cooling method and system having high efficiency |
| CN106115830A (en) * | 2016-08-05 | 2016-11-16 | 重庆市三耕储节能环保科技有限公司 | A kind of renewable sources of energy sea water automatic processing device |
| CN207212586U (en) * | 2017-07-28 | 2018-04-10 | 海南电网有限责任公司三沙供电局 | It is a kind of to utilize wind energy and the Sea Water Pumped Storage Station ship of solar energy |
| CN209010175U (en) * | 2018-06-01 | 2019-06-21 | 华北电力大学 | A kind of desalination plant cooperateing with solar energy and wind energy |
| CN210620293U (en) * | 2019-06-27 | 2020-05-26 | 中海油能源发展股份有限公司 | Salt water desalination system utilizing solar energy and wind energy |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114249334A (en) * | 2021-12-15 | 2022-03-29 | 唐山市银海食盐有限公司 | Wind, light and electricity complementary system for processing granular sea salt |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5399565B2 (en) | Combined cycle power plant using solar heat | |
| CN102010020B (en) | Solar energy sea water desalinization heat collecting system | |
| CN101708871B (en) | Gradient preheating multistage evaporation-type seawater desalination power generation system | |
| CN210620293U (en) | Salt water desalination system utilizing solar energy and wind energy | |
| CN101973598A (en) | Spray evaporating air-moistening de-humidity type solar sea water desalinating device | |
| CN103670554B (en) | Power generation and heat supply device | |
| CN109867317A (en) | A kind of efficient cryogenic atomization injection desalination plant and its method | |
| CN109734240A (en) | A kind of seawater desalination system and desalination method | |
| CN103265140A (en) | Solar line focusing-wind energy synergetic ultrasonic sea water desalting device and method | |
| CN207943899U (en) | A kind of MVR seawater desalination systems | |
| CN103775029B (en) | waste heat recovery liquid nitrogen evaporating system | |
| CN110272080A (en) | It is a kind of using solar energy and the salt water desalination system of wind energy | |
| CN203428942U (en) | Evaporative condensation type sea water desalination device | |
| CN105329962B (en) | Solar energy composite heat pump desalinization and confession domestic water system and method | |
| CN208395002U (en) | Multifunctional seawater desalting energy-saving environmental protection device | |
| CN208312760U (en) | Three combined production device of solar refrigeration supplying hot water and fresh water | |
| EP3334907B1 (en) | Thermodynamic engine | |
| CN203256082U (en) | Solar ray light condensation-wind energy synergistic ultrasonic seawater desalination device | |
| CN109354095A (en) | Intelligent solar water trichotomy desalination plant | |
| CN105756732B (en) | A kind of LNG/ liquid oxygen direct combustion Mixed working fluid cycle TRT | |
| CN104326519A (en) | Evaporative condensation type sea water desalination device | |
| CN206889110U (en) | It is a kind of to integrate efficient, economize on water, the controllable co-generation system of gas turbine four | |
| CN110526318A (en) | A kind of flue gas disappears the total energy approach method and system of white coupling sea water desalination | |
| CN105423623A (en) | Sewage heating heat pump capable of replacing large-sized heating boiler | |
| JP5422746B2 (en) | Solar thermal gas turbine plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |