CN207091042U - Desalinization evaporator - Google Patents
Desalinization evaporator Download PDFInfo
- Publication number
- CN207091042U CN207091042U CN201720983228.6U CN201720983228U CN207091042U CN 207091042 U CN207091042 U CN 207091042U CN 201720983228 U CN201720983228 U CN 201720983228U CN 207091042 U CN207091042 U CN 207091042U
- Authority
- CN
- China
- Prior art keywords
- evaporator
- water tank
- condensation
- pipe
- concentrated water
- 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
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Classifications
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- 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
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses desalinization evaporator, including evaporator, condensation water tank, with concentrated water case, the condensation water tank is between evaporator and concentrated water case, the bottom of the evaporator is provided with heater, escape pipe is connected with the top of the evaporator, and escape pipe is provided with the first valve, the side of the evaporator is provided with water inlet, and the opposite side of evaporator is respectively equipped with concentrated water outlet and steam (vapor) outlet, the steam (vapor) outlet is connected with steam pipe, the one end of the steam pipe away from evaporator is connected with condenser, and junction is the import of condenser, the outlet of the condenser is connected with condensation water tank by the first steel pipe and connected with condensation water tank, the side of the condensation water tank, which is located at below the junction of the first steel pipe and condensation water tank, offers two the first apertures.The utility model is thermally formed vapor by being carried out to seawater, is carrying out condensation to vapor so that the effect of the desalination of seawater.
Description
Technical field
It the utility model is related to field of sea water desalting technology, more particularly to desalinization evaporator.
Background technology
It is also fewer and fewer with the waste freshwater resources of water resource, to reduce the waste of water resource, promote water circulation use,
Various water treatment facilities are widely used, and sphere area distribution situation is shown over the ground, and ocean area occupies the ratio of maximum,
But due to substantial amounts of salt component and other impurities in seawater be present, people can not directly drink, and be this it is proposed that seawater is light
Change evaporator.
The content of the invention
The purpose of this utility model is to solve shortcoming present in prior art, and the desalinization proposed is evaporated
Device.
To achieve these goals, the utility model employs following technical scheme：
Desalinization evaporator, including evaporator, condensation water tank and concentrated water case, the condensation water tank are located at evaporator
Between concentrated water case, the bottom of the evaporator is provided with heater, and escape pipe, and outlet are connected with the top of the evaporator
Pipe is provided with the first valve, and the side of the evaporator is provided with water inlet, and the opposite side of evaporator is respectively equipped with concentrated water outlet
And steam (vapor) outlet, the steam (vapor) outlet are connected with steam pipe, the one end of the steam pipe away from evaporator is connected with condenser, and
Junction is the import of condenser, and the outlet of the condenser is connected with condensation water tank by the first steel pipe and connected with condensation water tank
Logical, the side of the condensation water tank, which is located at below the junction of the first steel pipe and condensation water tank, offers two the first apertures,
The opposite side of condensation water tank offers condensation-water drain, is respectively connected with the first tubule on two first apertures, and first is thin
The one end of pipe away from condensation water tank is connected with feed pump, the second valve is equipped with first tubule, and the second valve is located at
Between condensation water tank and feed pump, the outlet of two feed pumps is respectively connected with the second tubule, and two second tubules are remote
One end from feed pump connects with steam pipe and circulating pump respectively, and the inlet and outlet of the circulating pump are distinguished by two second steel pipes
Exporting in concentrated water and connected with concentrated water case, second steel pipe is provided with circulation pipe, and the steel pipe of circulation pipe second forms three-port structure,
The circulation pipe is between circulating pump and concentrated water case, and circulation pipe and the second steel pipe junction are provided with triple valve, the concentrated water
The inside of case is provided with dividing plate, and overfall is offered on the dividing plate, and the inside of the concentrated water case is provided with dividing plate, opened on the dividing plate
Provided with overfall.
Preferably, the bottom of the concentrated water case is provided with supporting leg, and one end that second tubule connects with steam pipe, which is fixed, to be connected
It is connected to micropore shower nozzle.
Preferably, the height of the condensation-water drain is more than the first tubule and the height of condensation water tank junction.
Preferably, the position height that the height of the junction of the steam pipe and evaporator is more than water inlet and concentrated water exports
Degree.
Preferably, the bottom of the concentrated water case offers concentrated water outlet.
In the utility model, by the way that the seawater by pretreatment to be discharged into the inside of evaporator by water inlet, then cold
Injected clear water is heated by heater to the seawater inside evaporator to the position of condensation-water drain in condensation tank, with
The rise of the temperature inside evaporator, seawater will evaporate to form vapor, and vapor enters steam pipe by steam (vapor) outlet
Condensed water is just formed into condenser and is discharged into condensation water tank, while opens the second valve successively and starts feed pump, circulating pump, is given
Water pump throws the clear water in condensation water tank into the inside of steam pipe in the form of spraying, and accelerates steam to form condensed water, while cold
Clear water in condensation tank, which can be also injected at the rotary shaft of circulating pump, prevents that running produces high temperature and damaged circulating pump for a long time, with
Substantial amounts of concentrate can be produced by the bottom of the increase evaporator of evaporation capacity, now open triple valve, and circulation pipe is in closing
Concentrate will be drained into concentrated water case by concentrated water outlet, so can effectively realize to enter substantial amounts of seawater by state, circulating pump
Row evaporation, improve the operating efficiency of equipment.
Brief description of the drawings
Fig. 1 be the utility model proposes desalinization evaporator structural representation.
In figure：1 evaporator, 2 heaters, 3 water inlets, 4 first valves, 5 escape pipes, 6 steam pipes, 7 second valves
Door, 8 feed pumps, 9 condensers, 10 condensation-water drains, 11 condensation water tanks, 12 overfalls, 13 second tubules, 14 circulating pumps,
15 first steel pipes, the outlet of 16 concentrated waters, 17 concentrated water casees, 18 circulation pipes, 19 triple valves.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole
Embodiment.
Reference picture 1, desalinization evaporator, including evaporator 1, condensation water tank 11 and concentrated water case 17, condensation water tank 11
Between evaporator 1 and concentrated water case 17, the bottom of evaporator 1 is provided with heater 2, and the top of evaporator 1 is connected with outlet
Pipe 5, and escape pipe 5 is provided with the first valve 4, the side of evaporator 1 is provided with water inlet 3, and the opposite side of evaporator 1 is set respectively
There are concentrated water outlet 16 and steam (vapor) outlet, steam (vapor) outlet to be connected with steam pipe 6, the one end of steam pipe 6 away from evaporator 1 is connected with cold
Condenser 9, and junction be condenser 9 import, the outlet of condenser 9 be connected by the first steel pipe 15 with condensation water tank 11 and with
Condensation water tank 11 connects, and the side of condensation water tank 11 is located at the first steel pipe 15 with being offered below the junction of condensation water tank 11
Two the first apertures, the opposite side of condensation water tank 11 offer condensation-water drain 10, first are respectively connected with two the first apertures
Tubule, and the one end of the first tubule away from condensation water tank 11 is connected with feed pump 8, and the second valve 7 is equipped with the first tubule, and
Second valve 7 is between condensation water tank 11 and feed pump 8, and the outlets of two feed pumps 8 is respectively connected with the second tubule 13, two
Second one end of tubule 13 away from feed pump 8 connects with steam pipe 6 and circulating pump 14 respectively, and the inlet and outlet of circulating pump 14 pass through two
The steel pipe of root second connects respectively at concentrated water outlet 16 and concentrated water case 17, and the second steel pipe is provided with circulation pipe 18, and circulation pipe 18 the
Two steel pipes form three-port structure, and circulation pipe 18 is between circulating pump 14 and concentrated water case 17, and the steel pipe of circulation pipe 18 and second is handed over
Meet place and be provided with triple valve 19, the inside of concentrated water case 17 is provided with dividing plate, and the inside that the concentrated water case 17 of overfall 12 is offered on dividing plate is set
There is dividing plate, overfall 12 is offered on dividing plate.
In the present embodiment, by the way that the seawater by pretreatment to be discharged into the inside of evaporator 1 by water inlet 3, then cold
Injected clear water is added to the position of condensation-water drain 10 by heater 2 to the seawater inside evaporator 1 in condensation tank 11
Heat, with the rise of the temperature inside evaporator 1, seawater will be evaporated to form vapor, and vapor is entered by steam (vapor) outlet
Steam pipe 6 enters condenser 9, and just formation condensed water is discharged into condensation water tank 11, while opens the second valve 7 successively and start feedwater
Pump 8, circulating pump 14, feed pump 8 throw the clear water in condensation water tank 11 into the inside of steam pipe 6 in the form of spraying, and accelerate to steam
Vapour forms condensed water, while the clear water in condensation water tank 11 can also be injected at the rotary shaft of circulating pump 14 and prevent circulating pump 14 from growing
Time running produces high temperature and damaged, and as the bottom of the increase evaporator 1 of evaporation capacity can produce substantial amounts of concentrate, now will
Triple valve 19 is opened, and circulation pipe 18 is in closed state, and concentrate will be drained into concentrated water by circulating pump 14 by concentrated water outlet 16
Case 17, it so can effectively realize and substantial amounts of seawater is evaporated, improve the operating efficiency of equipment.
It is described above, the only preferable embodiment of the utility model, but the scope of protection of the utility model is not
This is confined to, any one skilled in the art is in the technical scope that the utility model discloses, according to this practicality
New technical scheme and its utility model design are subject to equivalent substitution or change, should all cover in protection model of the present utility model
Within enclosing.
Claims (5)
1. desalinization evaporator, including evaporator（1）, condensation water tank（11）And concentrated water case（17）, it is characterised in that institute
State condensation water tank（11）Positioned at evaporator（1）With concentrated water case（17）Between, the evaporator（1）Bottom be provided with heater
（2）, the evaporator（1）Top be connected with escape pipe（5）, and escape pipe（5）It is provided with the first valve（4）, the evaporation
Tank（1）Side be provided with water inlet（3）, and evaporator（1）Opposite side be respectively equipped with concentrated water outlet（16）And steam (vapor) outlet, institute
State steam (vapor) outlet and be connected with steam pipe（6）, the steam pipe（6）Away from evaporator（1）One end be connected with condenser（9）, and
Junction is condenser（9）Import, the condenser（9）Outlet pass through the first steel pipe（15）With condensation water tank（11）Connection
And and condensation water tank（11）Connection, the condensation water tank（11）Side be located at the first steel pipe（15）With condensation water tank（11）Company
Two the first apertures, condensation water tank are offered below the place of connecing（11）Opposite side offer condensation-water drain（10）Described in two
The first tubule is respectively connected with first aperture, and the first tubule is away from condensation water tank（11）One end be connected with feed pump（8）, institute
State and the second valve is equipped with the first tubule（7）, and the second valve（7）Positioned at condensation water tank（11）And feed pump（8）Between, two
The individual feed pump（8）Outlet be respectively connected with the second tubule（13）, two second tubules（13）Away from feed pump（8）'s
One end respectively with steam pipe（6）And circulating pump（14）Connection, the circulating pump（14）Inlet and outlet pass through two second steel pipes point
Do not exported with concentrated water（16）With concentrated water case（17）Connection, second steel pipe are provided with circulation pipe（18）, and circulation pipe（18）The
Two steel pipes form three-port structure, the circulation pipe（18）Positioned at circulating pump（14）With concentrated water case（17）Between, and circulation pipe（18）
Triple valve is provided with the second steel pipe junction（19）, the concentrated water case（17）Inside be provided with dividing plate, offered on the dividing plate
Overfall（12）.
2. desalinization evaporator according to claim 1, it is characterised in that the concentrated water case（17）Bottom be provided with
Supporting leg, second tubule and steam pipe（6）One end of connection is fixedly connected with micropore shower nozzle.
3. desalinization evaporator according to claim 1, it is characterised in that the condensation-water drain（10）Height
More than the second tubule and condensation water tank（11）The height of junction.
4. desalinization evaporator according to claim 1, it is characterised in that the steam pipe（6）With evaporator（1）
The height of junction be more than water inlet（3）Exported with concentrated water（16）Position height.
5. desalinization evaporator according to claim 1, its feature exist, the concentrated water case（17）Bottom offer
Concentrated water exports.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720983228.6U CN207091042U (en) | 2017-08-08 | 2017-08-08 | Desalinization evaporator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720983228.6U CN207091042U (en) | 2017-08-08 | 2017-08-08 | Desalinization evaporator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207091042U true CN207091042U (en) | 2018-03-13 |
Family
ID=61544171
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720983228.6U Expired - Fee Related CN207091042U (en) | 2017-08-08 | 2017-08-08 | Desalinization evaporator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207091042U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116986661A (en) * | 2023-09-26 | 2023-11-03 | 南京沿江资源生态科学研究院有限公司 | Multistage coupling and separating device for organic waste liquid |
-
2017
- 2017-08-08 CN CN201720983228.6U patent/CN207091042U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116986661A (en) * | 2023-09-26 | 2023-11-03 | 南京沿江资源生态科学研究院有限公司 | Multistage coupling and separating device for organic waste liquid |
| CN116986661B (en) * | 2023-09-26 | 2023-12-15 | 南京沿江资源生态科学研究院有限公司 | Multistage coupling and separating device for organic waste liquid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180313 Termination date: 20180808 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |