CN105836829A - Sleeve type fresh water sea salt coproduction system - Google Patents
Sleeve type fresh water sea salt coproduction system Download PDFInfo
- Publication number
- CN105836829A CN105836829A CN201610409117.4A CN201610409117A CN105836829A CN 105836829 A CN105836829 A CN 105836829A CN 201610409117 A CN201610409117 A CN 201610409117A CN 105836829 A CN105836829 A CN 105836829A
- Authority
- CN
- China
- Prior art keywords
- fresh water
- accumulation layer
- sea
- heating cylinder
- water accumulation
- 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.)
- Granted
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
- C02F1/045—Treatment of water, waste water, or sewage by heating by distillation or evaporation for obtaining ultra-pure water
-
- 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
- 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
- C02F1/047—Treatment of water, waste water, or sewage by heating by distillation or evaporation using eolic energy
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
- F03B—MACHINES OR ENGINES FOR LIQUIDS
- F03B13/00—Adaptations of machines or engines for special use; Combinations of machines or engines with driving or driven apparatus; Power stations or aggregates
- F03B13/12—Adaptations of machines or engines for special use; Combinations of machines or engines with driving or driven apparatus; Power stations or aggregates characterised by using wave or tide energy
- F03B13/26—Adaptations of machines or engines for special use; Combinations of machines or engines with driving or driven apparatus; Power stations or aggregates characterised by using wave or tide energy using tide energy
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
- F03D—WIND MOTORS
- F03D9/00—Adaptations of wind motors for special use; Combinations of wind motors with apparatus driven thereby; Wind motors specially adapted for installation in particular locations
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
- F03D—WIND MOTORS
- F03D9/00—Adaptations of wind motors for special use; Combinations of wind motors with apparatus driven thereby; Wind motors specially adapted for installation in particular locations
- F03D9/008—Adaptations of wind motors for special use; Combinations of wind motors with apparatus driven thereby; Wind motors specially adapted for installation in particular locations the wind motor being combined with water energy converters, e.g. a water turbine
-
- 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
- C02F2303/00—Specific treatment goals
- C02F2303/10—Energy recovery
-
- 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
- Y02E10/30—Energy from the sea, e.g. using wave energy or salinity gradient
-
- 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
- Y02E10/72—Wind turbines with rotation axis in wind direction
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Hydrology & Water Resources (AREA)
- Power Engineering (AREA)
- Sustainable Energy (AREA)
- Sustainable Development (AREA)
- Oceanography (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses a sleeve type fresh water sea salt coproduction system, which comprises a heating cylinder (5), a seawater storage layer (3) and a fresh water storage layer (2) in sequential arrangement from inside to outside, wherein a sealing piston (15) capable of doing vertical and reciprocating movement is arranged inside the heating cylinder (5); a piston rod of the sealing piston (15) sequentially passes out of the top ends of the heating cylinder (5), the seawater storage layer (3) and the fresh water storage layer (2) to be connected with a mechanical transmission mechanism (14); the bottom of the heating cylinder (5) is of a funnel-shaped structure; the funnel-shaped structure sequentially passes through the back ends of the seawater storage layer (3) and the fresh water storage layer (2), and then, an opening is right aligned with a salt storage tank (9); a sweater inlet and a water vapor outlet (7) are formed in the wall of the heating cylinder (5). The sleeve type fresh water sea salt coproduction system provided by the invention has the advantages that materials are taken in site; reproducible energy sources are used in a way of taking actions that suit local circumstances to realize the combined production of fresh water and sea salt; the structure is compact; the cost is low; the energy is saved; the environment is protected.
Description
Technical field
The present invention relates to a kind of telescopic fresh water sea salt co-generation system, belong to renewable energy utilization technical field.
Background technology
Along with socioeconomic development, traditional fossil energy is the most exhausted, and environmental pollution is on the rise, and uses the production of renewable energy resources life of cleanliness without any pollution to be vigorously advocated and put into practice.At present, desalination technology is varied, including hyperfiltration, electroosmose process, pressure steam distillation method, some evaporation etc., these methods and technology are respectively arranged with the pluses and minuses of oneself, and many counting methods and technology simply are solely used for producing fresh water, solve the awkward situation that fresh water is nervous, and have ignored the utilization of sea salt.The preparation of sea salt has much prospects for commercial application, can meet industrial salt demand.
Summary of the invention
The technical problem to be solved is to provide a kind of compact conformation, can Joint Production fresh water and the telescopic fresh water sea salt co-generation system of sea salt；Further, the present invention provides a kind of various green resource Joint Production fresh water that can utilize seashore and the telescopic fresh water sea salt co-generation system of sea salt；Further, the present invention provides one efficiently to utilize the energy, and the fresh water speed of response is fast, the telescopic fresh water sea salt co-generation system that output efficiency is high.
For solving above-mentioned technical problem, the technical solution used in the present invention is:
A kind of telescopic fresh water sea salt co-generation system, including the heating cylinder set gradually from inside to outside, sea water accumulation layer and fresh water accumulation layer, described heating cylinder is internally provided with the sealing piston that can pump, and the piston rod of described sealing piston passes described heating cylinder successively, sea water accumulation layer is connected with mechanical transmission mechanism behind the top of fresh water accumulation layer；Being funnel-shaped structure bottom described heating cylinder, described funnel-shaped structure passes the bottom after-opening of described sea water accumulation layer and fresh water accumulation layer successively just to storage salt cellar；Sea intake and steam outlet it is provided with on the wall of described heating cylinder, described steam outlet is connected with described fresh water accumulation layer by check valve after running through described sea water accumulation layer, described sea intake is connected with described sea water accumulation layer by flow control valve, described heating cylinder outer wall circumference is gathered electrical heating wire, described fresh water accumulation layer top is provided with air bleeding valve, described fresh water accumulation layer bottom is provided with water outlet, described sea water accumulation layer is provided with Mare Frigoris water inlet, and described Mare Frigoris water inlet is connected with the external world after running through described fresh water accumulation layer.
Described Mare Frigoris water inlet is positioned at the top of described sea water accumulation layer, and described sea intake and steam outlet are respectively positioned on the middle and lower part of described heating cylinder.
Described mechanical transmission mechanism is connected with rotating blower fan.
Described electrical heating wire is connected with tidal power unit.
It is provided with some fin on described fresh water accumulation layer outer wall.
Described Mare Frigoris water inlet is connected with seawater treatment apparatus.
The opening part of described funnel-shaped structure is provided with hermatic door.
Described tidal power unit includes hydraulic generator.
Described sealing piston is inverted T-shape structure.
The one telescopic fresh water sea salt co-generation system that the present invention provides, sets gradually heating cylinder, sea water accumulation layer and the design of fresh water accumulation layer from inside to outside, and making the present invention is telescoping structure, compact conformation, and miniaturization, floor space is little；The setting of funnel-shaped structure, makes the present invention can be used to produce and collect sea salt, it is achieved that fresh water and the Joint Production of sea salt；Tidal power unit and rotate the setting of blower fan, makes the present invention gather materials on the spot, utilizes regenerative resource (including wind energy and tide energy) Joint Production fresh water and sea salt treatment in accordance with local conditions, and compact conformation is with low cost, energy-conserving and environment-protective；Sea water accumulation layer is positioned at outside heating cylinder, and heating cylinder outer wall circumference is gathered the setting of electrical heating wire, sea water accumulation layer absorbs the heat of the steam of fresh water accumulation layer and the outer wall heat of electrical heating wire simultaneously, the sea water to be diluted making the present invention has preheating function, when sea water to be diluted is after sea water accumulation layer becomes temperature sea water, enters heating cylinder heating and concentrates, decrease energy expenditure and the sea water concentration time of electrical heating wire, efficiently utilizing the energy, the fresh water speed of response is fast, and output efficiency is high.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Detailed description of the invention
Below in conjunction with the accompanying drawings the present invention is further described.
As it is shown in figure 1, a kind of telescopic fresh water sea salt co-generation system, including heating cylinder 5, sea water accumulation layer 3 and fresh water accumulation layer 2.The sealing piston 15 that can pump is installed at heating cylinder 5 top, is distributed holes below heating cylinder 5, and a hole is sea intake, and another hole is steam outlet 7, and making bottom heating cylinder 5 can the funnel-shaped structure of discharging.Sea water accumulation layer 3 is wrapped in heating cylinder 5, the wherein densely covered electrical heating wire 4 of circumference.Flow control valve 10 is connected with heating cylinder 5, and steam outlet 7 is connected with check valve 6.Fresh water accumulation layer 2 is wrapped in sea water accumulation layer 3.
Heating cylinder 5 is a hollow type cylinder body, and cylinder base is funnel-shaped structure, can open the salt unloading precipitation bottom funnel-shaped structure.Being distributed holes below heating cylinder 5, a hole is sea intake and is connected with flow control valve 10, and another hole is steam outlet 7 and is connected with check valve 6.
Sea water accumulation layer 3 is wrapped in heating cylinder 5, is enclosed within the outside of heating cylinder 5.A hole is opened in sea water accumulation layer 3 upper end, as Mare Frigoris water inlet 16.Circumferentially wound electrical heating wire 4 in sea water accumulation layer 3, the electric energy that electrical heating wire 4 consumes comes from tidal power unit.Tidal power unit is hydraulic generator 12.
Fresh water accumulation layer 2 is wrapped in sea water accumulation layer 3, is the outermost layer of whole system.Condensed fresh water equipped with a valve, for water outlet 8, can be released by fresh water accumulation layer 2 upper end equipped with an air bleeding valve 1, bottom.The outside finned 11 of fresh water accumulation layer 2.
Sealing piston 15 is inverted T-shape structure, is arranged on heating cylinder 5 upper end, can pump in heating cylinder 5, drives the mechanical transmission mechanism 14 sealing piston 15 up and down motion to be connected with rotating blower fan 13.
Equipped with seawater treatment apparatus before Mare Frigoris water inlet 16, sea water can be filtered, the pretreatment such as disinfection.
It is internal that flow control valve 10 is arranged on sea water accumulation layer 3, connects with heating cylinder 5, controls to enter the sea water amount within heating cylinder 5.
Steam outlet 7 is connected with check valve 6, and check valve 6 is arranged in fresh water accumulation layer 2, it is ensured that the water vapour only export but no import in heating cylinder 5, unidirectional discharge.
The innovative point of the present invention have following some: 1. utilize the Renewable resource on seashore, it is achieved zero-emission, contamination-freely produce sea salt, energy-saving and emission-reduction；2. apply in fresh water sea salt joint production process after " the four-stroke combustion pattern " of explosive motor being improved；3. compact conformation, Automation of Manufacturing Process, improves production efficiency.
The present invention gathers materials on the spot, and utilizes regenerative resource (including wind energy and tide energy) Joint Production fresh water and sea salt treatment in accordance with local conditions, and compact conformation is with low cost, energy-conserving and environment-protective.
The operation principle labor of the present invention is as follows:
Flowing into sea water accumulation layer 3 through pretreated sea water of technique such as filtration, sterilizings from Mare Frigoris water inlet 16, control to enter the sea water amount in heating cylinder 5 by flow control valve 10, after a small amount of sea water enters, flow control valve 10 cuts out.Now, sealing piston 15 and move upward under the driving of mechanical transmission mechanism 14, owing to being confined space in heating cylinder 5, in heating cylinder 5, pressure reduces suddenly, and the boiling point of water certainly will reduce.Before this, electrical heating wire 4 heating cylinder body in sea water accumulation layer 3, temperature in heating cylinder 5 raises, and reaches the boiling point of water after cylinder internal drop, and instant water is vaporized into steam.Afterwards, sealing piston 15 and move downward under the driving of mechanical transmission mechanism 14, in heating cylinder 5, pressure raises, and check valve 6 is opened under the extruding of water vapour in cylinder, and water vapour is discharged in fresh water accumulation layer 2 be condensed into fresh water.During water vapour condensation, partial heat is passed to the sea water in sea water accumulation layer 3, save the electric energy that electrical heating wire 4 consumes.The execution that above procedure is gone round and begun again, along with the discharge of water vapour, necessarily separates out more salt, now, opens the funnel bottom heating cylinder 5 in heating cylinder 5, salt is collected in storage salt cellar 9 under gravity.Mechanical transmission mechanism 14 is connected with rotating blower fan 13, is converted to wind energy seal the mechanical energy that piston 15 moves up and down, and the electric energy that electrical heating wire 4 consumes comes from hydraulic generator 12.
The above is only the preferred embodiment of the present invention; it is noted that, for those skilled in the art; under the premise without departing from the principles of the invention, it is also possible to make some improvements and modifications, these improvements and modifications also should be regarded as protection scope of the present invention.
Claims (9)
1. a telescopic fresh water sea salt co-generation system, it is characterized in that: include heating cylinder (5), sea water accumulation layer (3) and the fresh water accumulation layer (2) set gradually from inside to outside, described heating cylinder (5) is internally provided with the sealing piston (15) that can pump, and the piston rod of described sealing piston (15) passes described heating cylinder (5) successively, sea water accumulation layer (3) is connected with mechanical transmission mechanism (14) with behind the top of fresh water accumulation layer (2)；Described heating cylinder (5) bottom is funnel-shaped structure, and described funnel-shaped structure passes the bottom after-opening of described sea water accumulation layer (3) and fresh water accumulation layer (2) successively just to storage salt cellar (9)；Sea intake and steam outlet (7) it is provided with on the wall of described heating cylinder (5), described steam outlet (7) is run through described sea water accumulation layer (3) and is connected with described fresh water accumulation layer (2) by check valve (6) afterwards, described sea intake is connected with described sea water accumulation layer (3) by flow control valve (10), described heating cylinder (5) outer wall circumference is gathered electrical heating wire (4), described fresh water accumulation layer (2) top is provided with air bleeding valve (1), described fresh water accumulation layer (2) bottom is provided with water outlet (8), described sea water accumulation layer (3) is provided with Mare Frigoris water inlet (16), described Mare Frigoris water inlet (16) is run through described fresh water accumulation layer (2) and is connected with the external world afterwards.
One the most according to claim 1 telescopic fresh water sea salt co-generation system, it is characterized in that: described Mare Frigoris water inlet (16) is positioned at the top of described sea water accumulation layer (3), described sea intake and steam outlet (7) and is respectively positioned on the middle and lower part of described heating cylinder (5).
One the most according to claim 1 telescopic fresh water sea salt co-generation system, it is characterised in that: described mechanical transmission mechanism (14) is connected with rotating blower fan (13).
One the most according to claim 1 telescopic fresh water sea salt co-generation system, it is characterised in that: described electrical heating wire (4) is connected with tidal power unit.
One the most according to claim 1 telescopic fresh water sea salt co-generation system, it is characterised in that: it is provided with some fin (11) on described fresh water accumulation layer (2) outer wall.
One the most according to claim 1 telescopic fresh water sea salt co-generation system, it is characterised in that: described Mare Frigoris water inlet (16) is connected with seawater treatment apparatus.
One the most according to claim 1 telescopic fresh water sea salt co-generation system, it is characterised in that: the opening part of described funnel-shaped structure is provided with hermatic door.
One the most according to claim 4 telescopic fresh water sea salt co-generation system, it is characterised in that: described tidal power unit includes hydraulic generator (12).
One the most according to claim 1 telescopic fresh water sea salt co-generation system, it is characterised in that: described sealing piston (15) is inverted T-shape structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610409117.4A CN105836829B (en) | 2016-06-12 | 2016-06-12 | A kind of telescopic fresh water sea salt co-generation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610409117.4A CN105836829B (en) | 2016-06-12 | 2016-06-12 | A kind of telescopic fresh water sea salt co-generation system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105836829A true CN105836829A (en) | 2016-08-10 |
| CN105836829B CN105836829B (en) | 2018-06-05 |
Family
ID=56576724
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610409117.4A Expired - Fee Related CN105836829B (en) | 2016-06-12 | 2016-06-12 | A kind of telescopic fresh water sea salt co-generation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105836829B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107487803A (en) * | 2017-09-16 | 2017-12-19 | 侯梦斌 | A kind of wind energy evaporation equipment and technique for intervening NACF plate |
| CN109956509A (en) * | 2017-12-25 | 2019-07-02 | 北京佑陆科技有限公司 | The seawater desalination system based on open type Stirling cycle driven by wind energy conversion system |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004076359A1 (en) * | 2003-02-26 | 2004-09-10 | Sven Olof Sonander | Water desalination |
| CN1994901A (en) * | 2006-12-21 | 2007-07-11 | 上海交通大学 | Portable hand-pressurized heat pump sea water desalination barrel |
| WO2010045892A1 (en) * | 2008-10-23 | 2010-04-29 | Branlay Capital Holding Ltd | Method and device for desalinating and/or purification of water |
| CN202880936U (en) * | 2012-09-12 | 2013-04-17 | 海南大学 | Sea water desalting device |
| CN103387270A (en) * | 2013-07-18 | 2013-11-13 | 海南大学 | A vacuum vapor compression distillation sea water desalination device |
| KR101610596B1 (en) * | 2015-08-13 | 2016-04-07 | 박정원 | The sea water desalination apparatus |
-
2016
- 2016-06-12 CN CN201610409117.4A patent/CN105836829B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004076359A1 (en) * | 2003-02-26 | 2004-09-10 | Sven Olof Sonander | Water desalination |
| CN1994901A (en) * | 2006-12-21 | 2007-07-11 | 上海交通大学 | Portable hand-pressurized heat pump sea water desalination barrel |
| WO2010045892A1 (en) * | 2008-10-23 | 2010-04-29 | Branlay Capital Holding Ltd | Method and device for desalinating and/or purification of water |
| CN202880936U (en) * | 2012-09-12 | 2013-04-17 | 海南大学 | Sea water desalting device |
| CN103387270A (en) * | 2013-07-18 | 2013-11-13 | 海南大学 | A vacuum vapor compression distillation sea water desalination device |
| KR101610596B1 (en) * | 2015-08-13 | 2016-04-07 | 박정원 | The sea water desalination apparatus |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107487803A (en) * | 2017-09-16 | 2017-12-19 | 侯梦斌 | A kind of wind energy evaporation equipment and technique for intervening NACF plate |
| CN107487803B (en) * | 2017-09-16 | 2020-07-24 | 侯梦斌 | Wind energy evaporation equipment and process for inserting activated carbon fiber plate |
| CN109956509A (en) * | 2017-12-25 | 2019-07-02 | 北京佑陆科技有限公司 | The seawater desalination system based on open type Stirling cycle driven by wind energy conversion system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105836829B (en) | 2018-06-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105836829A (en) | Sleeve type fresh water sea salt coproduction system | |
| CN106213987B (en) | A kind of Steam Recovery reutilization system | |
| CN105952586A (en) | Multi-energy assisted fresh water and sea salt co-production system | |
| CN209752529U (en) | Organic waste gas recycling device | |
| CN103644030B (en) | A kind of solar automobile power source using medium heat absorption and energy recovery internal combustion engine | |
| CN103277212B (en) | A kind of supercritical internal combustion direct-flow steam cluster engine | |
| CN112973317A (en) | Tail gas treatment equipment for chemical production | |
| CN105936520B (en) | A kind of electric heating piston reciprocating type seawater desalination system | |
| CN215864784U (en) | Gas boiler waste heat recycling equipment | |
| CN201485899U (en) | Device for generating fresh water | |
| CN106150936A (en) | A kind of solar energy thermo-motor | |
| CN108866886A (en) | A kind of textile printing and dyeing drying machine device for recycling condensed water and its application method | |
| CN204986937U (en) | Industrial solar energy steam generator | |
| CN209084738U (en) | A kind of oxygen-eliminating device steam exhaust recovering device | |
| CN204126763U (en) | A kind of silicone core bundling tube external-burning engine | |
| CN103423021B (en) | A kind of novel to spray rotator type external-combustion engine cylinder and to spray rotator type external-combustion engine | |
| CN203959979U (en) | A kind ofly utilize the solar powered energy-conservation water system of making | |
| CN207963175U (en) | Device is absorbed and utilized in a kind of boiler emission hot water thermal energy | |
| CN208536641U (en) | Condensed water active recyclable device | |
| CN102213487A (en) | Pneumatic wind-driven heating device based on reverse Stirling cycle | |
| CN1422811A (en) | Solar seawater purifier | |
| CN206987973U (en) | A kind of automobile engine shell with radiating and moisture-proof function | |
| CN109362344B (en) | Driving device for applying hydrogen energy new energy to rice harvester | |
| CN209978047U (en) | Energy-saving industrial waste incineration system | |
| CN209494671U (en) | A kind of energy-saving cooling system of wind-driven generator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180605 Termination date: 20210612 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |