CN104973640A - Seawater desalination salt collector - Google Patents
Seawater desalination salt collector Download PDFInfo
- Publication number
- CN104973640A CN104973640A CN201510420981.XA CN201510420981A CN104973640A CN 104973640 A CN104973640 A CN 104973640A CN 201510420981 A CN201510420981 A CN 201510420981A CN 104973640 A CN104973640 A CN 104973640A
- Authority
- CN
- China
- Prior art keywords
- water
- heating container
- fresh water
- liquidometer
- collecting
- 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
-
- 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
-
- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention relates to a seawater desalination salt collector which is characterized by comprising a heat collecting rack, a heating box and a fresh water collecting box, wherein the heat collecting rack is uniformly distributed and provided with parabolic mirrors; a heat collecting tube is arranged on the parabolic mirrors, and both ends of the heat collecting tube are connected with two liquid pumps; and the two liquid pumps are connected through a circulating pipeline which penetrates through the heating box. Compared with the prior art, the solar energy is utilized to heat the heat-conducting oil, and can maximally heat the heat-conducting oil in the heat collecting tube to 400 DEG C; the seawater in the heating box is heated and distilled through the circulating pipeline, thereby saving the energy; and the collector is simple and convenient, has the advantages of small appearance, small occupied area and energy saving, and is green and environment-friendly since all the energies are supplied by solar energies.
Description
Technical field
The invention belongs to environmental protection machinery technical field, be specifically related to a kind of sea water desaltination and receive salt device.
Background technology
Namely sea water desaltination utilizes sea water desalinization to produce fresh water.Be the increment technique of increasing income realizing water resources utilization, fresh water total amount can be increased, and not by space-time and weather effect, the stable water supply such as coastal Drinking Water for Residents and Industrial Boiler moisturizing can be ensured.
The process meaning sea water desaltination of fresh water is obtained from seawater.Method for desalting seawater now used have seawater freezing method,
electroosmose process, distillation method,
reverse osmosis method, apply at present
reverse osmosis membranereverse osmosis method simple with its equipment, be easy to safeguard and the advantage of EM equipment module dominates the market rapidly, progressively replace
distillationmethod becomes most widely used method.
There are 100 Duo Ge scientific research institutions of more than ten country in the world in the research carrying out sea water desaltination, have the sea water desaltination facility of hundreds of different structure and differing capacities in work.One modern large-scale
desalimtor, several thousand, several ten thousand even nearly 1,000,000 tons of fresh water can be produced every day.The cost of desalination water is constantly reducing, and some country has been reduced to the price difference of tap water few.The desalination water yield of certain areas reaches the water supply scale in country and city.
A kind of thermal power generation of Patent publication No CN102040258A and the method for distillation seawater desalination coproduction, from temperature of power plant steam turbine intermediate pressure cylinder final stage extraction section steam, first base turbine generating is entered, discharge after distributing electricity, enter distillation sea water desalting device and carry out sea water desaltination as heating steam.The invention also discloses the equipment of a kind of thermal power generation and distillation seawater desalination coproduction, comprise the power station generator of temperature of power plant steam turbine and driving thereof, temperature of power plant steam turbine is connected with condenser of power plant, this equipment also comprises the generator of base turbine and driving thereof, the inlet mouth of base turbine is connected with the intermediate pressure cylinder final stage of temperature of power plant steam turbine, and the venting port of base turbine is connected with distillation sea water desalting device.The present invention can reduce the cost being supplied to desalination by distillation factory steam, and that finally reduces sea water desaltination makes water cost; Meanwhile, the scale of sea water desaltination can be determined as required, be realized by adjustment steam extracted amount, make the water yield not by the restriction of steam turbine scale.
And for example a kind of sea water desaltination of Patent publication No CN203333431U and the integration unit of strong brine utilization, comprise renewable energy power generation device, control device, sea water desalinating plant and strong brine and utilize device, described renewable energy power generation device utilizes device to power to control device, sea water desalinating plant and strong brine, control device controls the operation that renewable energy power generation device, sea water desalinating plant and strong brine utilize device to power, and strong brine take-off equipment and the strong brine of described sea water desalinating plant utilize device to be connected.
At present, receive salt device at existing solar seawater desalination and be mainly divided into two large types: 1, passive type solar energy Distallation systm main drawback: 1) latent heat of steam is not re-used; 2) thermal capacity of seawater is too large; 3) in device, natural convection pattern limits the raising of device performance; 2, active solar energy Distallation systm main drawback: 1) equipment cost is relatively high; 2) need to expend certain electric energy, be unfavorable for that outlying islander uses.Meanwhile, above-mentioned two kinds of modes all need to consume electric energy and desalinate to drive equipment operation, and can consume mass energy like this, for underway boats and ships and marine island, burden is larger like this.
Summary of the invention
The present invention is directed to the shortcoming of prior art, propose sea water desaltination and receive salt device, this device, is distilled seawater heat-conducting oil heating by sun power, produces fresh water, and speed is fast, does not need the energy, environmental protection.
For realizing object of the present invention, the technical solution used in the present invention is:
Salt device is received in sea water desaltination, it is characterized in that: comprise thermal-arrest frame, heating container and fresh water collecting case, uniformly on described thermal-arrest frame is provided with parabolic lens; Thermal-collecting tube is arranged on above parabolic lens, and its two ends are connected with liquid absorbing pump, and described liquid absorbing pump quantity is 2, is connected with the circulating line through described heating container between the two;
Described heating container top droop is provided with the cloth that catchments, water delivery bar is connected to below the cloth that catchments, immediately below described water delivery bar, fresh water collecting conduit is installed, fresh water collecting conduit is parallel to each other with the cloth that catchments and arranges, described fresh water collecting conduit lower end is communicated with collecting pipe, and described collecting pipe is communicated with water shoot; Described heating container is provided with inclined ramp, receives the side that salt box abuts against inclined ramp.Described inclined ramp top is connected with gassing pipe, and receive on salt box and be provided with connector link, gassing pipe is connected with outside air pump.
Described water shoot is connected with fresh water collecting case, water transfer pump is arranged on heating container, is connected with water-supply line between water transfer pump and heating container, and described heating container is provided with liquidometer, be connected with signal transmission line between water transfer pump and liquidometer, rising pipe is connected to below fresh water collecting case.
Preferentially, also comprise signal projector, described signal projector and be all connected with signal line group between water transfer pump and liquidometer.Described liquid level counts electronic liquid level gauge.
Preferentially, described fresh water collecting case is also provided with liquidometer, between liquidometer and signal projector, is connected with signal transmission line.
Preferentially, described water delivery bar extends downwardly into fresh water collecting conduit inside.
Preferentially, described circulating line is provided with lateral in heating container inside, and described lateral is uniform to be connected to below circulating line.
Compared with prior art, advantage of the present invention is: adopt sun power to heat thermal oil, the highlyest by the heat-conducting oil heating in thermal-collecting tube to 400 degree, can add thermal distillation by circulating line to the seawater in heating container, the saving energy; Device is easy, low-profile, and floor space is little has energy-saving effect, and whole energy is provided by sun power, environmental protection.
Accompanying drawing explanation
The following accompanying drawing by means of embodiment carries out brief description to the present invention now.In accompanying drawing:
Fig. 1 shows the structural arrangement schematic diagram that salt device is received in sea water desaltination of the present invention;
Fig. 2 shows the structural arrangement schematic diagram of thermal-arrest frame of the present invention;
Fig. 3 shows heating container inside top figure of the present invention.
Embodiment
Below in conjunction with specific embodiment, the present invention is described in detail.Following examples will contribute to those skilled in the art and understand the present invention further, but not limit the present invention in any form.It should be pointed out that to those skilled in the art, without departing from the inventive concept of the premise, some distortion and improvement can also be made.These all belong to protection scope of the present invention.
Embodiment 1
As shown in the figure, salt device is received in sea water desaltination, comprises thermal-arrest frame 3, heating container 13 and fresh water collecting case 19, uniformly on described thermal-arrest frame 3 is provided with parabolic lens 6; Thermal-collecting tube 5 is arranged on above parabolic lens 6, and its two ends are connected with liquid absorbing pump 1, and described liquid absorbing pump 1 quantity is 2, is connected with the circulating line 10 through described heating container 13 between the two.Liquid absorbing pump 1 outside is provided with regulating gate 2, parabolic lens 6 is circular arc, and multiple parabolic lens 6 installs integrated formation circular arc by collection sheet 9, and to be locked with collection sheet 9 by screw 8 and be connected and fixed, parabolic lens 6 two ends are laid with pilot hole 7 by axle center, for regulating thermal-collecting tube 5 deviation angle.
Described heating container 13 top droop is provided with the cloth 18 that catchments, and water delivery bar 14 is connected to below the cloth 18 that catchments, and it is inner that water delivery bar 14 extends downwardly into fresh water collecting conduit 21.Catchment cloth 18 and water delivery bar 14 material is nylon, and be provided with fresh water collecting conduit 21 immediately below described water delivery bar 14, the cross section of fresh water collecting conduit 21 is arc, material selection aluminium.Fresh water collecting conduit 21 is parallel to each other with both the cloth 18 that catchments and arranges, described fresh water collecting conduit 21 lower end is communicated with collecting pipe 22, and described collecting pipe 22 is communicated with water shoot 12.Circulating line 10 is provided with lateral 24 in heating container 13 inside, and described lateral 24 is uniform to be connected to below circulating line 10, and circulating line 10 and lateral 24 preferentially adopt copper pipe.Be provided with inclined ramp 17 bottom described heating container 13, receive salt box 23 and abut against inclined ramp 17 side, it is multiple for receiving salt box 23 quantity, and uniform movable is arranged, it is wooden for receiving salt box 23.Described inclined ramp 17 top is connected with gassing pipe 26, and receive on salt box 23 and be provided with connector link 25, gassing pipe 26 is connected and uniform layout with outside air pump.
Water shoot 12 is connected with fresh water collecting case 19, water transfer pump 15 is arranged on heating container 13, water-supply line is connected with between water transfer pump 15 and heating container 13, described heating container 13 is provided with liquidometer 11, be connected with signal transmission line 50 between water transfer pump 15 and liquidometer 11, rising pipe 20 is connected to below fresh water collecting case 19.Also comprise signal projector 16, described signal projector 16 and be all connected with signal line group between water transfer pump 15 and liquidometer 11.Described liquidometer 11 is electronic liquid level gauge.In addition, fresh water collecting case 19 is also provided with liquidometer, between liquidometer and signal projector 16, is connected with signal transmission line.
Salt device is received in this sea water desaltination disclosed by the invention, principle of work is such, first in heating container 13, carries seawater by water transfer pump 15, and water transfer pump 15 is PLC control motor, liquidometer 11 is sensed water level height automatically, and the moment sends information to water transfer pump 15.Be marked with thermal oil in thermal-collecting tube 5 simultaneously, the heat of sun power focuses on thermal-collecting tube 5 and heats thermal oil by parabolic lens 6, thermal oil is the highest is heated to 400 degrees Celsius, the thermal oil of heating is sent in circulating line 10 by liquid absorbing pump 1, it is heating of seawater that such thermal oil enters in heating container 13, makes its generation steam that seethes with excitement.
Steam moves upward and condensation forms fresh water on the cloth 18 that catchments, owing to catchmenting, cloth 18 is in tilted layout, then fresh water is constantly to its low side diffluence, water declines to entering in fresh water collecting conduit 21 along water delivery bar 14 and arrives collecting pipe 22 again and assemble in flow process, fresh water in collecting pipe 22 enters in water shoot 12 again, fresh water enters in fresh water collecting case 19 eventually through water shoot 12 to be assembled, if desired fresh water is used, discharged by rising pipe 20, rising pipe 20 is above provided with hand door, controlledly makes water size.Meanwhile, the continuous crystallization of the salinity in seawater, blow automatically to be blown into receive in salt box 23 by gassing pipe 26 timing and assemble, staff regularly opens heating container 13 and clears up.
Claims (5)
1. salt device is received in sea water desaltination, it is characterized in that: comprise thermal-arrest frame (3), heating container (13) and fresh water collecting case (19), and described thermal-arrest frame (3) is above uniform is provided with parabolic lens (6); Thermal-collecting tube (5) is arranged on above parabolic lens (6), and its two ends are connected with liquid absorbing pump (1), and described liquid absorbing pump (1) quantity is 2, is connected with the circulating line (10) through described heating container (13) between the two;
Described heating container (13) top droop is provided with the cloth that catchments (18), water delivery bar (14) is connected to the cloth that catchments (18) below, immediately below described water delivery bar (14), fresh water collecting conduit (21) is installed, fresh water collecting conduit (21) is parallel to each other with both the cloth (18) that catchments and arranges, described fresh water collecting conduit (21) lower end is communicated with collecting pipe (22), and described collecting pipe (22) is communicated with water shoot (12); Described heating container (13) bottom is provided with inclined ramp (17), receive salt box (23) and abut against ramp inclination ramp (17) side, described inclined ramp (17) top is connected with gassing pipe (26), receive on salt box (23) and be provided with connector link (25), gassing pipe (26) is connected with outside air pump;
Described water shoot (12) is connected with fresh water collecting case (19), water transfer pump (15) is arranged on heating container (13), water-supply line is connected with between water transfer pump (15) and heating container (13), described heating container (13) is provided with liquidometer (11), be connected with signal transmission line (50) between water transfer pump (15) and liquidometer (11), rising pipe (20) is connected to fresh water collecting case (19) below.
2. salt device is received in sea water desaltination according to claim 1, it is characterized in that: also comprise signal projector (16), described signal projector (16) and be all connected with signal line group between water transfer pump (15) and liquidometer (11).
3. salt device is received in sea water desaltination according to claim 1 and 2, it is characterized in that: described liquidometer (11) is electronic liquid level gauge.
4. salt device is received in sea water desaltination according to claim 1 and 2, it is characterized in that: it is inner that described water delivery bar (14) extends downwardly into fresh water collecting conduit (21).
5. salt device is received in sea water desaltination according to claim 1, it is characterized in that: described circulating line (10) is provided with lateral (24) in heating container (13) inside, and described lateral (24) is uniform is connected to circulating line (10) below.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510420981.XA CN104973640B (en) | 2015-07-17 | 2015-07-17 | Salt device is received in desalinization |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510420981.XA CN104973640B (en) | 2015-07-17 | 2015-07-17 | Salt device is received in desalinization |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104973640A true CN104973640A (en) | 2015-10-14 |
| CN104973640B CN104973640B (en) | 2017-12-08 |
Family
ID=54270672
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510420981.XA Active CN104973640B (en) | 2015-07-17 | 2015-07-17 | Salt device is received in desalinization |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104973640B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105928046A (en) * | 2016-04-29 | 2016-09-07 | 浙江海洋大学 | Heating and ventilating control system for buildings and heat supply method of heating and ventilating control system |
Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1785826A (en) * | 2005-10-30 | 2006-06-14 | 梁嘉麟 | Sea water evaporator for making sea water continuously evaporate in desalination process |
| CN101017029A (en) * | 2007-03-05 | 2007-08-15 | 云南师范大学 | Channel light gathering solar energy reflexion heat collection device |
| DE102008042069A1 (en) * | 2008-09-12 | 2010-03-18 | Deutsche Institute Für Textil- Und Faserforschung Denkendorf | Apparatus for recovering a liquid from an aerosol |
| CN102336449A (en) * | 2010-07-18 | 2012-02-01 | 刘方旭 | Device for desalinating seawater and brackish water by solar energy and wind energy, and displacement method |
| CN102798242A (en) * | 2012-07-23 | 2012-11-28 | 泰州市华源供热工程有限公司 | Reflection type solar support |
| CN102849813A (en) * | 2012-08-29 | 2013-01-02 | 集美大学 | Solar multi-effect distillation system |
| CN202735581U (en) * | 2012-09-07 | 2013-02-13 | 卢正杰 | Solar energy collecting device |
| CN202912730U (en) * | 2012-09-28 | 2013-05-01 | 童东华 | Marine sea water desalinization device |
| CN103641194A (en) * | 2013-12-10 | 2014-03-19 | 天津城建大学 | Solar seawater concentration desalting device and method |
| CN103693795A (en) * | 2013-12-04 | 2014-04-02 | 浙江海洋学院 | Household type solar seawater desalting system |
| CN103967075A (en) * | 2013-01-29 | 2014-08-06 | 北京大学 | Porous fine denier nylon fiber used for water collection |
| CN204848327U (en) * | 2015-07-17 | 2015-12-09 | 舟山市智海技术开发有限公司 | Seawater desalination receives salt device |
-
2015
- 2015-07-17 CN CN201510420981.XA patent/CN104973640B/en active Active
Patent Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1785826A (en) * | 2005-10-30 | 2006-06-14 | 梁嘉麟 | Sea water evaporator for making sea water continuously evaporate in desalination process |
| CN101017029A (en) * | 2007-03-05 | 2007-08-15 | 云南师范大学 | Channel light gathering solar energy reflexion heat collection device |
| DE102008042069A1 (en) * | 2008-09-12 | 2010-03-18 | Deutsche Institute Für Textil- Und Faserforschung Denkendorf | Apparatus for recovering a liquid from an aerosol |
| CN102336449A (en) * | 2010-07-18 | 2012-02-01 | 刘方旭 | Device for desalinating seawater and brackish water by solar energy and wind energy, and displacement method |
| CN102798242A (en) * | 2012-07-23 | 2012-11-28 | 泰州市华源供热工程有限公司 | Reflection type solar support |
| CN102849813A (en) * | 2012-08-29 | 2013-01-02 | 集美大学 | Solar multi-effect distillation system |
| CN202735581U (en) * | 2012-09-07 | 2013-02-13 | 卢正杰 | Solar energy collecting device |
| CN202912730U (en) * | 2012-09-28 | 2013-05-01 | 童东华 | Marine sea water desalinization device |
| CN103967075A (en) * | 2013-01-29 | 2014-08-06 | 北京大学 | Porous fine denier nylon fiber used for water collection |
| CN103693795A (en) * | 2013-12-04 | 2014-04-02 | 浙江海洋学院 | Household type solar seawater desalting system |
| CN103641194A (en) * | 2013-12-10 | 2014-03-19 | 天津城建大学 | Solar seawater concentration desalting device and method |
| CN204848327U (en) * | 2015-07-17 | 2015-12-09 | 舟山市智海技术开发有限公司 | Seawater desalination receives salt device |
Non-Patent Citations (1)
| Title |
|---|
| 韩广甸 等: "《有机制备化学手册（上卷）》", 31 January 1977 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105928046A (en) * | 2016-04-29 | 2016-09-07 | 浙江海洋大学 | Heating and ventilating control system for buildings and heat supply method of heating and ventilating control system |
| CN105928046B (en) * | 2016-04-29 | 2018-08-17 | 浙江海洋大学 | Building HVAC regulator control system and its heating method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104973640B (en) | 2017-12-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102642883B (en) | System for desalinating seawater by waste heat from power plant | |
| CN102336448B (en) | Saline treatment system and method | |
| CN204848326U (en) | Solar seawater desalts power generation facility for boats and ships | |
| CN104986818A (en) | Solar seawater desalination and electricity generation apparatus for ships | |
| CN103964527B (en) | One solar seawater desalination factory | |
| CN102329035B (en) | Fresh water collecting and supplying system | |
| CN105060380A (en) | Solar seawater desalination and power generation device for ship | |
| CN101205087A (en) | Highly effective sea-water brackish water distillatory using renewable energy | |
| CN101838024A (en) | Driven flash-evaporation solar seawater desalination method and device | |
| CN203781962U (en) | Household solar-powered seawater desalination system | |
| CN201834781U (en) | Single-stage vacuum distillation seawater desalination device | |
| CN201660457U (en) | Novel multiple-effect distilled sea water desalination device | |
| CN204848327U (en) | Seawater desalination receives salt device | |
| CN108275738A (en) | MVR seawater desalination systems based on generation of electricity by new energy | |
| CN105060379A (en) | Seawater desalination and salt collection device | |
| CN106966462A (en) | A kind of multistage seawater desalting coupled system | |
| CN104973640A (en) | Seawater desalination salt collector | |
| CN207608448U (en) | Utilize the seawater desalination system of power station thermal energy production and living water | |
| Mabrouk et al. | Experimental evaluation of novel hybrid multi effect distillation–membrane distillation (MED-MD) driven by solar energy | |
| CN105036225A (en) | Marine seawater desalination and salt recovery apparatus | |
| CN204848325U (en) | Seawater desalination equipment | |
| CN204918044U (en) | Solar seawater desalts power generation facility for boats and ships | |
| CN204824240U (en) | Solar energy sea water desalination apparatus | |
| CN103693795B (en) | Household type solar seawater desalting system | |
| CN105000614A (en) | Seawater desalination device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Han Jianjun Inventor after: Zhao Wenbing Inventor after: Dan Li Inventor after: Wang Yaohua Inventor after: Zhang Naiqian Inventor before: Zhao Xizeng |
|
| TA01 | Transfer of patent application right | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20171106 Address after: Ten road 257400 Shandong Lijin County of Dongying Province in the north of Tianjin city, Garden Road East Applicant after: Shandong Long Xiang Industrial Co., Ltd. Address before: Street peak village Dinghai District of Lincheng city of Zhoushan province Zhejiang 316000 Ni Jia No. 19 Applicant before: Zhoushan Zhihai Technology Development Co., Ltd. |
|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190916 Address after: 257 400 No. 102 Lishi Road, Lijin County, Dongying City, Shandong Province Patentee after: Dongying Xingsheng Special Equipment Technology Co., Ltd. Address before: Ten road 257400 Shandong Lijin County of Dongying Province in the north of Tianjin city, Garden Road East Patentee before: Shandong Long Xiang Industrial Co., Ltd. |