CN108083367A - A kind of small-sized solar desalination plant - Google Patents
A kind of small-sized solar desalination plant Download PDFInfo
- Publication number
- CN108083367A CN108083367A CN201711399247.5A CN201711399247A CN108083367A CN 108083367 A CN108083367 A CN 108083367A CN 201711399247 A CN201711399247 A CN 201711399247A CN 108083367 A CN108083367 A CN 108083367A
- Authority
- CN
- China
- Prior art keywords
- evaporation
- seawater
- condenser
- seawater tank
- pipe
- 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.)
- Withdrawn
Links
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
-
- 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
- C02F1/043—Details
-
- 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
-
- 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
- Y02A20/142—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
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
A kind of small-sized solar desalination plant provided by the invention, the water surface heating plate in evaporation of seawater tank convert solar energy into thermal energy evaporation seawater, and water vapour is condensed into water in condenser.Enter discharge pipe as seawater using a flexible hoses, have the multiple functions such as seawater entrance, seawater discharge, water level control concurrently, and it is easy to operate reliable.Make fresh water discharge pipe using a flexible hoses, condenser is made to have both water storage function.Air discharge duct is set in condenser and evaporation of seawater tank side, ensure that condenser will not be closed because of water storage, air hardly possible arranges and influences water vapour condensation.Air discharge duct and steam flow into pipe and are distributed in the two diagonal of evaporation of seawater tank, effectively exclude air, improve the exchange capability of heat of condenser.Therefore evaporation of seawater tank height is compressible within 20 centimetres, solar energy sea water desalination apparatus miniaturization target is accomplished.
Description
Technical field
The present invention relates to a kind of desalination plants, are specially a kind of small-sized solar desalination plant.
Background technology
Early in 16th century, Queen of England was just promulgated and ordered together:To inventing the people of cheap sea water desalination method, one is given
Ten thousand pounds of bonus.So far nobody obtains this bonus.British government announce queen then put on someone's head still effectively.2014
Year, developing low-cost sustainability desalination technology is also classified as one of sciences problems of six candidates by Britain's " longitude prize ".
Desalination technology development history is made a general survey of, although hot method, embrane method, ion-exchange, electroosmose process, hydrate, molten
The desalination technologies such as agent extraction continuously emerge, and desalination with Solar Energy is still in research and development and small-scale test rank
Section.But desalination with Solar Energy most possibly becomes inexpensive sustainability desalination technology.Because by the sea and
Island, solar energy enrich, and seawater is sufficient.It, just can be low as long as there is efficient solar energy sea water desalination apparatus to make full use of the two
A large amount of fresh water are produced into local.Chinese invention patent 201710028482.5 returns solar energy collecting, evaporation of seawater, condensation latent heat
Receipts are concentrated in an evaporation of seawater tank and completed, and latent heat evaporation seawater is recycled in tank.For desalination with Solar Energy
Open a new technology path.But the desalination with Solar Energy scheme is not preferred plan.The technical solution does not have
It solves the problems, such as to desalinize seawater using solar energy how to greatest extent, how do not find reduces device manufacturing cost direction,
The technical thought that solar energy is absorbed using evaporation of seawater tank side hinders solar energy sea water desalination apparatus to miniaturization.In sea
In water desalination process, the heat absorption of the hydrone of seawater surface becomes water vapour, water vapour in condenser exothermic condensation into liquid water,
Absorption by Sea Water thermal temperature rises.Solar energy needed for ocean temperature rising reduction hydrone vaporization, can evaporate more hydrones,
Be conducive to improve fresh water yield;Ocean temperature, which rises, also reduces water vapour and temperature difference of seawater, and the condensing capacity of condenser reduces, and has
It may cause part water vapour that can not be condensed into water, be expelled directly out desalination plant.So certainly exist a sea water temperature
Degree evaporates the water and the critical point holding balance of water vapour discharge desalination plant is condensate in water vapour.This ocean temperature
It is exactly the optimum operation temperature of solar energy sea water desalination apparatus.Solar energy sea water desalination apparatus is kept close to optimum operation temperature
Operation is reduced evaporation of seawater tank height, can just be desalinized seawater to greatest extent using solar energy and reduce device manufacturing cost, is realized
Solar energy sea water desalination apparatus minimizes.
The content of the invention
The purpose of the present invention is realizing solar energy sea water desalination apparatus miniaturization, design a kind of running temperature and connect as far as possible
The solar energy sea water desalination apparatus of nearly optimum operation temperature.
To achieve these goals, the scheme of the invention is:Its structure includes evaporation of seawater tank, condenser, seawater and flows into
Discharge pipe, water surface heating plate, steam flow into pipe, fresh water effuser, air discharge duct, stent.It is characterized in that:Evaporation of seawater tank
It is horizontally mounted on stent.Condenser is installed in bottom in evaporation of seawater tank.Water is placed between condenser and evaporation of seawater tank deck face
Face heating plate.Water surface heating plate is swum on the water surface of evaporation of seawater tank inland sea.Steam flows into pipe and connects condensation in condenser top surface
Device, steam flow into pipe import between water surface heating plate and evaporation of seawater tank deck face.Fresh water effuser is connected in condenser bottom surface
Condenser, fresh water effuser connect air through evaporation of seawater tank bottom face.Fresh water effuser outside evaporation of seawater tank is deformable
Hose, fresh water effuser are suspended on evaporation of seawater tank side.Fresh water effuser port position is higher than condenser top side location.It is empty
Gas discharge pipe connects condenser in condenser upper side, and air discharge duct connects air through evaporation of seawater tank side.Air
Discharge pipe and steam flow into pipe and are distributed in the two diagonal of evaporation of seawater tank.Seawater flows into discharge pipe and is connected in evaporation of seawater tank bottom face
Evaporation of seawater tank.It is flexible hoses that seawater, which flows into discharge pipe, and seawater flows into discharge pipe and is suspended on evaporation of seawater tank side.Sea
Water flows into discharge pipe port position and flows into pipe import less than steam, and it is evaporation of seawater tank inland sea that seawater, which flows into discharge pipe port position,
Water peak level.It is closed with transparent thermal insulation material in evaporation of seawater tank deck face.
The condenser is the hollow cylinder for having more two-ports in the heat exchanger tube of top and bottom, and condenser top surface connects
Steam flow into pipe, condenser upper side connection air discharge duct, condenser bottom surface connection fresh water effuser, steam flow into pipe with
It is two diagonal to be arranged in condenser for air discharge duct.
The evaporation of seawater tank deck face is made of transparent thermal insulation material.
The water surface heating plate is the microwell plate made of optothermal material.
The advantage of the invention is that:First, evaporation of seawater tank is highly compressible within 20 centimetres, device volume is small, structure
Compact, materials are few, and manufacture craft is simple, and manufacture is at low cost;Second is that a flexible hoses enter discharge pipe as seawater, sea is had concurrently
The multiple functions such as water entrance, seawater discharge, water level control, and it is easy to operate reliable;Third, a flexible hoses make fresh water
Discharge pipe makes condenser have both water storage function;Fourth, setting air discharge duct in condenser and evaporation of seawater tank side, ensure that cold
Condenser will not be closed because of water storage, and air hardly possible arranges and influences water vapour condensation;Fifth, air discharge duct flows into pipe distribution with steam
Two in evaporation of seawater tank are diagonal, effectively exclude air, improve the exchange capability of heat of condenser;Sixth, in device operational process,
There is no high temperature and pressure and " three wastes " discharge, safety and environmental protection.
Description of the drawings
The invention will be further described with embodiment below in conjunction with the accompanying drawings:
Fig. 1 is small-sized solar desalination plant figure of the present invention;
Fig. 2 is water surface heating plate of the present invention and condenser locations relational graph.
In figure, 1, evaporation of seawater tank, 2, seawater flow into discharge pipe, 3, air discharge duct, 4, stent, 5, fresh water effuser,
6th, water surface heating plate, 7, steam flow into pipe, 8, condenser, 9, heat exchanger tube.
Specific embodiment
The present embodiment is the small-sized solar seawater that 1 floor space of evaporation of seawater tank is 1 square metre, interior outage degree is 20 centimetres
Desalting plant.8 12 centimetres of height of condenser, interior empty 60 liters of volume.Peak level is located at 18 lis from tank bottom face in evaporation of seawater tank 1
At rice, that is, seawater flows into 18 centimetres from tank bottom face of 2 port position of discharge pipe.In this position, 1 volume 180 of evaporation of seawater tank
It rises, reduces empty 60 liters of volume in condenser 8, evaporation of seawater tank 1 is actual to hold 120 liters of seawater.Fig. 1 is the installation drawing of the present embodiment.
Evaporation of seawater tank 1 is horizontally mounted on stent 4, and condenser 8 is mounted on bottom in evaporation of seawater tank 1.Condenser 8 is that have more two
Port is in the hollow cylinder of the heat exchanger tube 9 of top and bottom.Steam flows into pipe 7 and connects condenser 8, steam in 8 top surface of condenser
Flow into 19 centimetres from tank bottom face of 7 import of pipe.Water surface heating plate 6 swims in the water surface.Fig. 2 describes steam and flows into 7 import of pipe, condensation
Position relationship between device 8, water surface heating plate.Fresh water effuser 5 connects condenser 8, fresh water effuser 5 in 8 bottom surface of condenser
Air is connected through evaporation of seawater tank bottom face, the fresh water effuser 5 outside evaporation of seawater tank 1 is flexible hoses, fresh water effuser 5
It is suspended on 1 side of evaporation of seawater tank, 5 port position of fresh water effuser is higher than 8 top side location of condenser.Air discharge duct 3 exists
8 upper side of condenser connects condenser 8, and air discharge duct 3 connects air through 1 side of evaporation of seawater tank.Air discharge duct 3
It is diagonally arranged that pipe 7 is flowed into steam.Seawater flows into discharge pipe 2 in 1 bottom surface of evaporation of seawater tank connection evaporation of seawater tank 1, seawater stream
It is flexible hoses to enter discharge pipe 2, and seawater flows into discharge pipe 2 and is suspended on evaporation of seawater tank side.1 top surface of evaporation of seawater tank is used
Transparent thermal insulation material is closed.
The present invention the course of work be:Seawater is flowed into 2 port of discharge pipe and is placed in highest water level, from seawater stream by early morning
Enter discharge pipe 2 and inject seawater, until seawater overflows.As the sun rises, sunlight is radiated at water surface heating plate 6 through transparent top
Its temperature is made to increase, the partial moisture son heat absorption in water surface heating plate 6 is vaporized into water vapour.Water vapour is by evaporation of seawater tank top
The air in space flows into pipe 7 through steam and squeezes into condenser 8, is then discharged to through air discharge duct 3 in air.Water vapour is in condenser
Water is condensed into 8, vapour latent heat is gradually increasing by Absorption by Sea Water, ocean temperature.After ocean temperature is raised to optimum operation temperature,
Water vapour is flowed out from air discharge duct 3.It reduces seawater and flows into 2 port of discharge pipe, discharge part seawater, then raise seawater and flow into row
2 port of outlet pipe, and normal temperature seawater is supplemented, water level is made to return to origin-location.If solar irradiation is insufficient, ocean temperature is always below
Optimum operation temperature, there is no need to replace part seawater.After the sun sets, seawater is flowed into 2 port of discharge pipe and drops to seawater steaming
It sends out below 1 bottom surface of tank, discharges whole seawater;5 port of fresh water effuser is dropped to below 1 bottom surface of evaporation of seawater tank, fresh water is natural
Solar seawater desalination is completed in outflow.
Claims (4)
1. a kind of small-sized solar desalination plant, including evaporation of seawater tank, condenser, seawater flows into discharge pipe, the water surface adds
Hot plate, steam flow into pipe, fresh water effuser, air discharge duct, stent, it is characterised in that:Evaporation of seawater tank is horizontally mounted in branch
On frame, condenser is installed in bottom in evaporation of seawater tank, and water surface heating plate, the water surface are placed between condenser and evaporation of seawater tank deck face
Heating plate is swum on the water surface of evaporation of seawater tank inland sea, and steam flows into pipe and connects condenser in condenser top surface, and steam flows into pipe
Between water surface heating plate and evaporation of seawater tank deck face, fresh water effuser connects condenser, fresh water stream in condenser bottom surface for import
Outlet pipe connects air through evaporation of seawater tank bottom face, and the fresh water effuser outside evaporation of seawater tank is flexible hoses, fresh water outflow
Pipe is suspended on evaporation of seawater tank side, and fresh water effuser port position is higher than condenser top side location, and air discharge duct is cold
Condenser upper side connects condenser, and air discharge duct connects air, air discharge duct and steam through evaporation of seawater tank side
It flowing into pipe and is distributed in the two diagonal of evaporation of seawater tank, seawater flows into discharge pipe and connects evaporation of seawater tank in evaporation of seawater tank bottom face,
It is flexible hoses that seawater, which flows into discharge pipe, and seawater flows into discharge pipe and is suspended on evaporation of seawater tank side, and seawater flows into discharge
Pipe port position flows into pipe import less than steam, and it is seawater highest water in evaporation of seawater tank that seawater, which flows into discharge pipe port position,
Position, evaporation of seawater tank deck face are closed with transparent thermal insulation material.
2. a kind of small-sized solar desalination plant according to claim 1, it is characterised in that:The condenser is that have
More two-ports are on the hollow cylinder of the heat exchanger tube of top and bottom, condenser top surface connection steam inflow pipe, condenser top
Side connects air discharge duct, condenser bottom surface connection fresh water effuser, and steam flows into pipe and is arranged in condensation with air discharge duct
The two of device are diagonal.
3. a kind of small-sized solar desalination plant according to claim 1, it is characterised in that:The evaporation of seawater tank
Top surface is made of transparent thermal insulation material.
4. a kind of small-sized solar desalination plant according to claim 1, it is characterised in that:The water surface heating plate
It is the microwell plate made of optothermal material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711399247.5A CN108083367A (en) | 2017-12-09 | 2017-12-09 | A kind of small-sized solar desalination plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711399247.5A CN108083367A (en) | 2017-12-09 | 2017-12-09 | A kind of small-sized solar desalination plant |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108083367A true CN108083367A (en) | 2018-05-29 |
Family
ID=62178450
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201711399247.5A Withdrawn CN108083367A (en) | 2017-12-09 | 2017-12-09 | A kind of small-sized solar desalination plant |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108083367A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111249757A (en) * | 2018-12-03 | 2020-06-09 | 中国科学院宁波材料技术与工程研究所 | Carbon fiber photothermal conversion material and application thereof in purification and recovery of multi-medium solvent |
CN111908541A (en) * | 2020-09-28 | 2020-11-10 | 荆门市润泽电磁脱盐设备有限公司 | Portable solar seawater desalination device |
-
2017
- 2017-12-09 CN CN201711399247.5A patent/CN108083367A/en not_active Withdrawn
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111249757A (en) * | 2018-12-03 | 2020-06-09 | 中国科学院宁波材料技术与工程研究所 | Carbon fiber photothermal conversion material and application thereof in purification and recovery of multi-medium solvent |
CN111908541A (en) * | 2020-09-28 | 2020-11-10 | 荆门市润泽电磁脱盐设备有限公司 | Portable solar seawater desalination device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4552208A (en) | Heat actuated system for circulating heat transfer fluids | |
CN201678475U (en) | Solar seawater desalination device | |
CN101481154A (en) | Method and apparatus for seawater desalination by comprehensive utilization of solar energy | |
KR20190067207A (en) | Sub-atmospheric heat and cold system | |
CN101993125A (en) | Solar vacuum seawater desalination device | |
JPS5820286A (en) | Sea water-desalinator using solar heat | |
CN104916334A (en) | Separated heat pipe type passive residual heat removal system for pressurized water reactor nuclear power plant | |
CN102910696A (en) | Solar seawater desalination device | |
KR100904308B1 (en) | Apparatus for taking fresh water from sea water using solar heat | |
CN109578974A (en) | A kind of boiler waste heat recovery system and energy-saving boiler system | |
CN108083367A (en) | A kind of small-sized solar desalination plant | |
CN106277137A (en) | Boats and ships solar seawater desalination TRT | |
CN107804887A (en) | A kind of method that seawater desalination system forms vacuum chamber | |
CN203560885U (en) | Continuous blowdown waste heat recovery system used for boiler | |
CN201140990Y (en) | All-glass vacuum heat-collection tube solar water purifier | |
CN102748963B (en) | Closed water cooling system with double-evaporative cooling pressure | |
CN204680390U (en) | Pressurized-water reactor nuclear power plant separate heat pipe formula Heat Discharging System of Chinese | |
CN106277123A (en) | Boats and ships solar seawater desalination TRT | |
CN101921005B (en) | Self-water storage type multi-stage vertical wall falling film condensation and distillation device | |
CN100488884C (en) | Hot vapour heating, heat siphon circulation submerged pipe type multi-effect evaporation desalting apparatus | |
US20140284201A1 (en) | Solar powered concentration unit and method of using solar power to concentrate a substance | |
CN209163543U (en) | A kind of air heat source and thermal pump swimming pool constant temperature system | |
EP2444665A1 (en) | Method for the natural draught cooling of a solar concentration plant | |
CN102180530B (en) | Device and method for sea water desalination by using solar energy and potential energy | |
CN111508624A (en) | Cooling system |
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 | ||
WW01 | Invention patent application withdrawn after publication | ||
WW01 | Invention patent application withdrawn after publication |
Application publication date: 20180529 |