CN206580586U - A kind of sea water desalinating unit - Google Patents

A kind of sea water desalinating unit Download PDF

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Publication number
CN206580586U
CN206580586U CN201720156015.6U CN201720156015U CN206580586U CN 206580586 U CN206580586 U CN 206580586U CN 201720156015 U CN201720156015 U CN 201720156015U CN 206580586 U CN206580586 U CN 206580586U
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CN
China
Prior art keywords
condensation
plenum chamber
output end
conduit
delivery port
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.)
Expired - Fee Related
Application number
CN201720156015.6U
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Chinese (zh)
Inventor
景传红
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dongguan Tide Water Treatment Technology Co Ltd
Original Assignee
Dongguan Tide Water Treatment Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Dongguan Tide Water Treatment Technology Co Ltd filed Critical Dongguan Tide Water Treatment Technology Co Ltd
Priority to CN201720156015.6U priority Critical patent/CN206580586U/en
Application granted granted Critical
Publication of CN206580586U publication Critical patent/CN206580586U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/138Water desalination using renewable energy
    • Y02A20/142Solar thermal; Photovoltaics
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/20Controlling water pollution; Waste water treatment
    • Y02A20/208Off-grid powered water treatment
    • Y02A20/212Solar-powered wastewater sewage treatment, e.g. spray evaporation

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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

The utility model discloses a kind of sea water desalinating unit, including suction pump, the water inlet end of suction pump is directly connected into seawater by pipeline, output end is connected with solar still, the output end of solar still is connected with the first condensation plenum chamber by conduit, the inside of first condensation plenum chamber, which is run through, condensation heat transfer pipe, condensation heat transfer pipe connects the input and output end of the first condensation plenum chamber, the output end of first condensation plenum chamber is provided with demister, first condensation plenum chamber gas outlet is connected to the second condensation plenum chamber by conduit, delivery port is connected to flash tank by conduit, the delivery port of second condensation plenum chamber is connected to flash tank by conduit, gas outlet is connected to the first condensation plenum chamber by feedback channel;The output end of flash tank is connected with afterbody condenser, and the upper end water outlet of afterbody condenser is connected with fresh water holding tank.The utility model can realize efficient sea water desalting, and the low transformation efficiency of energy consumption is high.

Description

A kind of sea water desalinating unit
Technical field
The utility model is related to field of sea water desalting technology, specially a kind of sea water desalinating unit.
Background technology
Desalinization produces fresh water using seawater desalination.It is to realize the increment technique of increasing income that water resource is utilized, Ke Yizeng Plus fresh water total amount, and not by space-time and climatic effect, the stable confession such as coastal Drinking Water for Residents and Industrial Boiler moisturizing can be ensured Water.In freshwater resources increasingly rare today, desalinization is undoubtedly the important channel for solving this problem, but existing sea The desalination inefficiency of water desalination apparatus typically, the energy of consumption is high, is unsuitable for promoting.
Utility model content
To achieve the above object, the utility model provides following technical scheme:A kind of sea water desalinating unit, including draw water Pump, the water inlet end of the suction pump is directly connected into seawater by pipeline, and output end is connected with solar still, it is described too The output end of positive energy evaporator is connected with the first condensation plenum chamber by conduit, and the inside of the first condensation plenum chamber, which is run through, to be had Condensation heat transfer pipe, the condensation heat transfer pipe connects the input and output end of the first condensation plenum chamber, the first condensation collection The output end of gas tank is provided with demister, and the output end of the first condensation plenum chamber is divided into gas outlet and delivery port, the gas outlet Second condensation plenum chamber is connected to by conduit, delivery port is connected to flash tank by conduit, the second condensation plenum chamber Delivery port is connected to flash tank by conduit, and gas outlet is connected to the first condensation plenum chamber by feedback channel;The flash tank Output end be connected with afterbody condenser, the upper end water outlet of the afterbody condenser is connected with fresh water holding tank.
As a kind of preferred technical scheme of the utility model, the solar still includes solar panel and steaming Kettle is sent out, the output end of the solar panel is connected with battery, and the output end of the battery is connected with electrothermal tube, described Electrothermal tube is evenly distributed on the inwall of evaporating kettle.
As a kind of preferred technical scheme of the utility model, the delivery port of the afterbody condenser bottom is connected with circulation Water pump, the other end of the water circulating pump is connected to the water inlet of solar still.
As a kind of preferred technical scheme of the utility model, the condensation heat transfer pipe and horizontal line into 45 degree of inclination angles to Under, gas outlet is located at top, and delivery port is located at bottom.
Compared with prior art, the beneficial effects of the utility model are:The sea water desalinating unit, by setting solar energy to steam Device is sent out, driving, clean environment firendly reduction energy consumption are used as by the use of solar power generation;Plenum chamber, the second condensation are condensed by setting first Plenum chamber, with reference to flash tank and afterbody condenser, is operated using multiple-effect evaporation condensation, so as to greatly improve desalinization utilization rate And efficiency;By set water circulating pump by incomplete desalination water be pumped into again solar still carry out circulating and evaporating operation, enter One step improves utilization ratio;The utility model can realize efficient sea water desalting, and the low transformation efficiency of energy consumption is high.
Brief description of the drawings
Fig. 1 is the utility model structural representation.
In figure:1- suction pumps;2- solar stills;3- first condenses plenum chamber;4- condensation heat transfer pipes;5- demisters; 6- gas outlets;7- delivery ports;8- second condenses plenum chamber;9- flash tanks;10- afterbody condensers;11- fresh water holding tanks;12- is followed Ring water pump;13- solar panels;14- batteries;15- electrothermal tubes;16- evaporating kettles.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made The every other embodiment obtained, belongs to the scope of the utility model protection.
Embodiment:
Referring to Fig. 1, the utility model provides a kind of technical scheme:A kind of sea water desalinating unit, including suction pump 1, institute The water inlet end for stating suction pump 1 is directly connected into seawater by pipeline, and output end is connected with solar still 2, the sun The output end of energy evaporator 2 is connected with the first condensation plenum chamber 3 by conduit, and the inside of the first condensation plenum chamber 3 is run through There is condensation heat transfer pipe 4, the condensation heat transfer pipe 4 connects the input and output end of the first condensation plenum chamber 3, and first is cold The output end of aggegation gas tank 3 is provided with demister 5, and the output end of the first condensation plenum chamber 3 is divided into gas outlet 6 and delivery port 7, institute State gas outlet 6 and second condensation plenum chamber 8 is connected to by conduit, delivery port 7 is connected to flash tank 9, described second by conduit The delivery port of condensation plenum chamber 8 is connected to flash tank 9 by conduit, and gas outlet is connected to the first condensation gas collection by feedback channel Case 3;The output end of the flash tank 9 is connected with afterbody condenser 10, the upper end water outlet connection of the afterbody condenser 10 There is fresh water holding tank 11.
The solar still 2 include solar panel 13 and evaporating kettle 16, the solar panel 13 it is defeated Go out end and be connected with battery 14, the output end of the battery 14 is connected with electrothermal tube 15, and the electrothermal tube 15 is evenly distributed on The inwall of evaporating kettle 16;The delivery port of the bottom of afterbody condenser 10 is connected with water circulating pump 12, the water circulating pump 12 The other end is connected to the water inlet of solar still 2;The condensation heat transfer pipe 4 and horizontal line are downward into 45 degree of inclination angles, outlet Mouth 6 is located at top, and delivery port 7 is located at bottom.
Seawater is directly drawn into solar still 2 by the suction pump 1, and the solar panel 13 is by solar energy Change into after electric energy and store to battery 14, then charged using battery 14 to electrothermal tube 15, electrothermal tube 15 and then heating production Raw high temperature gives the heat supply of evaporating kettle 16, so as to realize that heating evaporation is operated;Water vapour after evaporation enters the first condensation plenum chamber 3, By the down-film condenser in condensation heat transfer pipe 4, obtained condensed water enters demister 5, is removed by demister 5 after surfactant foam Enter second from delivery port 7 and condense plenum chamber 8, remaining vapor feeding second is condensed plenum chamber 8 and carries out two effects by gas outlet 6 Condensation operation, obtained condensed water enters flash tank 9, uncooled to be connected to the first condensation plenum chamber 3 by feedback channel and enter Row is circulated again;The flash tank 9 makes most of liquid moment produce flash distillation by reducing air pressure, and obtained vapor enters tail Portion's condenser 10 is stored in fresh water holding tank 11 after condensing;Non- evaporating completely by water circulating pump 12 is connected to solar still 2 circulate again.
Specifically used mode and advantage:The sea water desalinating unit, by setting solar still, utilizes solar power generation It is used as driving, clean environment firendly reduction energy consumption;Condense plenum chamber, the second condensation plenum chamber by setting first, with reference to flash tank and Afterbody condenser, is operated using multiple-effect evaporation condensation, so as to greatly improve desalinization utilization rate and efficiency;By setting circulation Incomplete desalination water is pumped into solar still progress circulating and evaporating operation by water pump again, further improves utilization ratio;This Utility model can realize efficient sea water desalting, and the low transformation efficiency of energy consumption is high.
It is obvious to a person skilled in the art that the utility model is not limited to the details of above-mentioned one exemplary embodiment, and And in the case of without departing substantially from spirit or essential attributes of the present utility model, can realize that this practicality is new in other specific forms Type.Therefore, no matter from the point of view of which point, embodiment all should be regarded as exemplary, and is nonrestrictive, this practicality is new The scope of type limits by appended claims rather than described above, it is intended that the equivalency fallen in claim is contained All changes in justice and scope are included in the utility model.Any reference in claim should not be considered as limitation Involved claim.

Claims (4)

1. a kind of sea water desalinating unit, it is characterised in that:Including suction pump(1), the suction pump(1)Water inlet end pass through pipeline It is directly connected into seawater, output end is connected with solar still(2), the solar still(2)Output end pass through Conduit is connected with the first condensation plenum chamber(3), the first condensation plenum chamber(3)Inside through there is condensation heat transfer pipe(4), institute State condensation heat transfer pipe(4)Plenum chamber is condensed by first(3)Input and output end connect, first condensation plenum chamber(3) Output end demister is installed(5), the first condensation plenum chamber(3)Output end be divided into gas outlet(6)And delivery port(7), institute State gas outlet(6)Second condensation plenum chamber is connected to by conduit(8), delivery port(7)Flash tank is connected to by conduit(9), The second condensation plenum chamber(8)Delivery port flash tank is connected to by conduit(9), gas outlet is connected to by feedback channel First condensation plenum chamber(3);The flash tank(9)Output end be connected with afterbody condenser(10), the afterbody condenser (10)Upper end water outlet be connected with fresh water holding tank(11).
2. a kind of sea water desalinating unit according to claim 1, it is characterised in that:The solar still(2)Including Solar panel(13)And evaporating kettle(16), the solar panel(13)Output end be connected with battery(14), institute State battery(14)Output end be connected with electrothermal tube(15), the electrothermal tube(15)It is evenly distributed on evaporating kettle(16)It is interior Wall.
3. a kind of sea water desalinating unit according to claim 1, it is characterised in that:The afterbody condenser(10)Bottom Delivery port is connected with water circulating pump(12), the water circulating pump(12)The other end be connected to solar still(2)Water inlet Mouthful.
4. a kind of sea water desalinating unit according to claim 1, it is characterised in that:The condensation heat transfer pipe(4)With level Line is downward into 45 degree of inclination angles, gas outlet(6)Positioned at top, delivery port(7)Positioned at bottom.
CN201720156015.6U 2017-02-21 2017-02-21 A kind of sea water desalinating unit Expired - Fee Related CN206580586U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720156015.6U CN206580586U (en) 2017-02-21 2017-02-21 A kind of sea water desalinating unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720156015.6U CN206580586U (en) 2017-02-21 2017-02-21 A kind of sea water desalinating unit

Publications (1)

Publication Number Publication Date
CN206580586U true CN206580586U (en) 2017-10-24

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Application Number Title Priority Date Filing Date
CN201720156015.6U Expired - Fee Related CN206580586U (en) 2017-02-21 2017-02-21 A kind of sea water desalinating unit

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI796449B (en) * 2018-05-08 2023-03-21 日商笹倉機械工程股份有限公司 Shipboard fresh water generation device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI796449B (en) * 2018-05-08 2023-03-21 日商笹倉機械工程股份有限公司 Shipboard fresh water generation device

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CF01 Termination of patent right due to non-payment of annual fee
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Granted publication date: 20171024

Termination date: 20190221