CN205222912U - Novel strong brine desalination equipment - Google Patents
Novel strong brine desalination equipment Download PDFInfo
- Publication number
- CN205222912U CN205222912U CN201520970587.9U CN201520970587U CN205222912U CN 205222912 U CN205222912 U CN 205222912U CN 201520970587 U CN201520970587 U CN 201520970587U CN 205222912 U CN205222912 U CN 205222912U
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- CN
- China
- Prior art keywords
- water
- strong brine
- vaporization chamber
- moisture condensation
- snakelike
- 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
Links
- 239000012267 brine Substances 0.000 title claims abstract description 48
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 title claims abstract description 48
- 238000010612 desalination reaction Methods 0.000 title abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 238000009833 condensation Methods 0.000 claims abstract description 33
- 230000005494 condensation Effects 0.000 claims abstract description 33
- 238000009834 vaporization Methods 0.000 claims abstract description 31
- 230000008016 vaporization Effects 0.000 claims abstract description 31
- 238000000889 atomisation Methods 0.000 claims description 25
- 239000003595 mist Substances 0.000 claims description 12
- 238000009692 water atomization Methods 0.000 claims description 10
- 238000007664 blowing Methods 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 claims description 4
- 239000011248 coating agent Substances 0.000 claims description 3
- 238000000576 coating method Methods 0.000 claims description 3
- 238000005260 corrosion Methods 0.000 claims description 3
- 230000007797 corrosion Effects 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 239000002184 metal Substances 0.000 abstract 2
- 239000006199 nebulizer Substances 0.000 abstract 2
- 238000000034 method Methods 0.000 description 15
- 238000004821 distillation Methods 0.000 description 6
- 239000012528 membrane Substances 0.000 description 6
- 238000001223 reverse osmosis Methods 0.000 description 6
- 239000013505 freshwater Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011033 desalting Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 235000019600 saltiness Nutrition 0.000 description 1
- XZPVPNZTYPUODG-UHFFFAOYSA-M sodium;chloride;dihydrate Chemical compound O.O.[Na+].[Cl-] XZPVPNZTYPUODG-UHFFFAOYSA-M 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model discloses an and provided a reasonable in design, simple structure, practically conveniently desaltd efficient, low cost and the novel strong brine desalination equipment of environmental protection. The utility model discloses a water supply nebulizer that connects gradually the setting constructs is equipped with vaporization cavity, steam condensation mechanism and the heat energy circulation metal group of high temperature heating board in, water supply nebulizer structure is connected with outside strong brine accumulator, steam condensation mechanism pass through heat energy circulation metal group with outside strong brine accumulator is connected. The utility model is suitable for a strong brine field of handling.
Description
Technical field
The utility model relates to a kind of Novel thick saline-water reclamation equipment.
Background technology
Strong brine can not be used directly because its saltiness is very high, main employing at present two kinds of methods desalinations strong brine, i.e. reverse osmosis membrane and distillation method.Reverse osmosis membrane applicable surface is very wide, and ratio of desalinization is very high, is therefore widely used.First reverse osmosis membrane is extracted by strong brine to carry out preliminary treatment, reduces strong brine turbidity, prevents the microbial growth such as bacterium, algae, then use the supercharging of Special high-voltage pump, make strong brine enter reverse osmosis membrane, finally draw standard compliant fresh water.But because reverse osmosis membrane desalination cannot process more than 50000ppm strong brine for concentration, therefore this method also has certain limitation.
Distillation method makes it boiling vaporization by heating strong brine, then vapor condensation is become the method for fresh water.Distillation method strong brine desalination techniques is the desalination techniques dropping into industrial applications the earliest, even if feature is also suitable in the strong brine environment of seriously polluted, high biological activity, it is high to produce water purity.Compared with reverse osmosis membrane strong brine desalination techniques, distillation method have can utilize power plant and other factories low-grade heat, to features such as raw material strong brine water quality requirement throughput that is low, device are large, be one of mainstream technology of current strong brine desalination.But the technique of current distillation method usually its heating fuel is all coal, low-quality fuel oil and other heavy contamination and the not high fuel of combustion utilization efficiency, again owing to being all adopt directly carry out heated and boiled to strong brine thus obtain water vapour, thus make that overall strong brine desalinating cost is high, inefficiency and contaminate environment.
Utility model content
Technical problem to be solved in the utility model overcomes the deficiencies in the prior art, provide a kind of reasonable in design, structure is simple, practical and convenient desalination efficiency is high, with low cost and the Novel thick saline-water reclamation equipment of environmental protection.
The technical scheme that the utility model adopts is: a kind of Novel thick saline-water reclamation equipment, it comprise connect successively arrange for water atomizing mechanism, in be provided with the vaporization chamber of heat plate, moisture condensation mechanism and snakelike moisture condensation pipe, the described water atomizing mechanism that supplies is connected with outside strong brine holder, and described moisture condensation mechanism is connected with described outside strong brine holder by described snakelike moisture condensation pipe.
Described vaporization chamber is corrosion resistant closed box, the right cabinet wall that described heat plate is fixedly installed on described vaporization chamber is connected with the green energy resource supply arrangement being arranged on described vaporization chamber outdoor, and the surface of described heat plate scribbles is not stained with salt coating.
Described vaporization chamber comprises atomization high-pressure pump and atomisation outlet, the feed-water end of described atomization high-pressure pump is connected with outside strong brine holder, described atomisation outlet is connected with the mist end that goes out of described atomization high-pressure pump, and described atomisation outlet is arranged on the bottom of the left side cabinet wall of described vaporization chamber and aims at described heat plate.
Described moisture condensation mechanism comprises blower, transfer of water vapour pipeline and water condensate storage case, the blowing mouth of described blower is arranged on the top of the left side cabinet wall of described vaporization chamber, described vaporization chamber is connected with described water condensate storage case by described transfer of water vapour pipeline, the admission end of described transfer of water vapour pipeline is arranged on the top of described vaporization chamber, the steam output end of described transfer of water vapour pipeline is arranged on the top of described water condensate storage case, one end of described snakelike moisture condensation pipe is arranged in described water condensate storage case, the other end is then connected with described outside strong brine holder.
Described admission end is provided with mist vapour separate mesh.
Described snakelike moisture condensation pipe inside is provided with heat transfer media.
The beneficial effects of the utility model are: in the utility model, owing to directly have employed the confession water atomizing mechanism connecting successively and arrange, vaporization chamber, moisture condensation mechanism and snakelike moisture condensation pipe, and wherein only include atomization high-pressure pump and atomisation outlet for water atomizing mechanism, vaporization chamber portion is only provided with heat plate, moisture condensation mechanism also only includes transfer of water vapour pipeline and water condensate storage case, so relative to desalting plant in the past, the structure of the Novel thick saline-water reclamation equipment in the utility model is simpler, manufacturing cost is cheaper, floor space is less and install and use convenient,
Owing to first have employed atomization high-pressure pump, high-pressure atomization is carried out to strong brine again, then the strong brine mist vapour of atomization is sprayed onto and is heated on the heat plate of more than 100 degrees Celsius, so the steam part in strong brine mist vapour can be made to evaporate more rapidly;
Again because the heat plate in the utility model adopts green energy resource to heat, and by snakelike moisture condensation pipe, the recycle heat that water of condensation condensation is distributed is sent in strong brine to be diluted, strong brine to be diluted is tentatively heated, thus make strong brine heating evaporation after atomization more quick, so the utility model is than strong brine distillation method environmental protection more in the past, efficiency is higher, cost is lower.
Accompanying drawing explanation
Fig. 1 is structural representation novel in the utility model.
Embodiment
As shown in Figure 1, a kind of Novel thick saline-water reclamation equipment, it comprise connect successively arrange for water atomizing mechanism, in be provided with the vaporization chamber 1 of heat plate 2, moisture condensation mechanism and snakelike moisture condensation pipe 5, the described water atomizing mechanism that supplies is connected with outside strong brine holder 7, and described moisture condensation mechanism is connected with described outside strong brine holder 7 by described snakelike moisture condensation pipe 5.Described snakelike moisture condensation pipe 5 inside is provided with heat transfer media.
Described vaporization chamber 1 is corrosion resistant closed box, and described vaporization chamber 1 is provided with evacuator.
On the right cabinet wall that described heat plate 2 is fixedly installed on described vaporization chamber 1 and by being arranged on the green energy resources such as the sun power of described vaporization chamber 1 outside, wind energy and water energy to carry out heat temperature raising, or it is also passable directly to connect common power supply.The surface of described heat plate 2 scribbles is not stained with salt coating.
Described comprising for water atomizing mechanism is atomized high-pressure pump 31 and atomisation outlet 32, the feed-water end of described atomization high-pressure pump 31 is connected with outside strong brine holder 7, described atomisation outlet 32 is connected with the mist end that goes out of described atomization high-pressure pump 31, and described atomisation outlet 32 is arranged on the bottom of the left side cabinet wall of described vaporization chamber 1 and aims at described heat plate 2.Described atomization high-pressure pump 31 can supply power with conventional power, also can use the green energy resource supply power such as sun power, wind energy and water energy.
Described moisture condensation mechanism comprises blower, transfer of water vapour pipeline 41 and water condensate storage case 42, the blowing mouth 43 of described blower is arranged on the top of the left side cabinet wall of described vaporization chamber 1, described vaporization chamber 1 is connected with described water condensate storage case 42 by described transfer of water vapour pipeline 41, and the admission end 44 of described transfer of water vapour pipeline 41 is arranged on the top of described vaporization chamber 1 and is provided with mist vapour separate mesh 45.The steam output end of described transfer of water vapour pipeline 41 is arranged on the top of described water condensate storage case 42, and the side of described water condensate storage case 42 is provided with and produces the mouth of a river 46.One end of described snakelike moisture condensation pipe 5 is arranged in described water condensate storage case 42, and the other end is then connected with described outside strong brine holder 7.
Principle of work:
The strong brine be stored in described outside strong brine holder 7 carries out extracting and being atomized by described atomization high-pressure pump 31, makes it form strong brine mist vapour.
Described strong brine mist vapour sprays to through described atomisation outlet 32 and contacts the described heat plate 2 completing heating, and the moisture in described strong brine mist vapour is flashed to water vapour by the high temperature that described heat plate 2 produces; The temperature of described heat plate 2 is greater than 100 degrees Celsius, has contacted unevaporated part in the described strong brine mist vapour of described heat plate 2 and has formed salt grain or the higher strong brine of concentration, finally dropped down onto the bottom of described vaporization chamber 1.Staff removes regularly carrying out collection to it.
Described water vapour enters described transfer of water vapour pipeline 41 through described admission end 44 under the effect of described blowing mouth 43, enter in described water condensate storage case 42 through described steam output end again, so described water vapour cool by described snakelike moisture condensation pipe 5 and be condensed into fresh water.
The heat of described water vapor condensation release is passed to described outside strong brine holder 7 through described snakelike moisture condensation pipe and tentatively heats the strong brine be stored in described outside strong brine holder 7.
The utility model is applicable to strong brine process field.
Claims (6)
1. a Novel thick saline-water reclamation equipment, it is characterized in that: it comprise connect successively arrange for water atomizing mechanism, in be provided with the vaporization chamber (1) of heat plate (2), moisture condensation mechanism and snakelike moisture condensation pipe (5), the described water atomizing mechanism that supplies is connected with outside strong brine holder, and described moisture condensation mechanism is connected with described outside strong brine holder by described snakelike moisture condensation pipe (5).
2. a kind of Novel thick saline-water reclamation equipment according to claim 1, it is characterized in that: described vaporization chamber (1) is corrosion resistant closed box, on the right cabinet wall that described heat plate (2) is fixedly installed on described vaporization chamber (1) and the green energy resource supply arrangement outside with being arranged on described vaporization chamber (1) be connected, the surface of described heat plate (2) scribbles is not stained with salt coating.
3. a kind of Novel thick saline-water reclamation equipment according to claim 2, it is characterized in that: described comprising for water atomizing mechanism is atomized high-pressure pump (31) and atomisation outlet (32), the feed-water end of described atomization high-pressure pump (31) is connected with outside strong brine holder, described atomisation outlet (32) is connected with the mist end that goes out of described atomization high-pressure pump (31), and described atomisation outlet (32) is arranged on the bottom of the left side cabinet wall of described vaporization chamber (1) and aims at described heat plate (2).
4. a kind of Novel thick saline-water reclamation equipment according to claim 1, it is characterized in that: described moisture condensation mechanism comprises blower, transfer of water vapour pipeline (41) and water condensate storage case (42), the blowing mouth (43) of described blower is arranged on the top of the left side cabinet wall of described vaporization chamber (1), described vaporization chamber (1) is connected with described water condensate storage case (42) by described transfer of water vapour pipeline (41), the admission end (44) of described transfer of water vapour pipeline (41) is arranged on the top of described vaporization chamber (1), the steam output end of described transfer of water vapour pipeline (41) is arranged on the top of described water condensate storage case (42), one end of described snakelike moisture condensation pipe (5) is arranged in described water condensate storage case (42), the other end is then connected with described outside strong brine holder.
5. a kind of Novel thick saline-water reclamation equipment according to claim 4, is characterized in that: described admission end (44) is provided with mist vapour separate mesh (45).
6. a kind of Novel thick saline-water reclamation equipment according to claim 1, is characterized in that: described snakelike moisture condensation pipe (5) inside is provided with heat transfer media.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520970587.9U CN205222912U (en) | 2015-11-30 | 2015-11-30 | Novel strong brine desalination equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520970587.9U CN205222912U (en) | 2015-11-30 | 2015-11-30 | Novel strong brine desalination equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205222912U true CN205222912U (en) | 2016-05-11 |
Family
ID=55897989
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520970587.9U Expired - Fee Related CN205222912U (en) | 2015-11-30 | 2015-11-30 | Novel strong brine desalination equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205222912U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105271593A (en) * | 2015-11-30 | 2016-01-27 | 珠海市江河海水处理设备工程有限公司 | Novel strong brine desalting equipment and novel strong brine desalting process |
-
2015
- 2015-11-30 CN CN201520970587.9U patent/CN205222912U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105271593A (en) * | 2015-11-30 | 2016-01-27 | 珠海市江河海水处理设备工程有限公司 | Novel strong brine desalting equipment and novel strong brine desalting process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160511 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |