CN203803293U - Steam-water pressurizing separation device - Google Patents
Steam-water pressurizing separation device Download PDFInfo
- Publication number
- CN203803293U CN203803293U CN201420168879.6U CN201420168879U CN203803293U CN 203803293 U CN203803293 U CN 203803293U CN 201420168879 U CN201420168879 U CN 201420168879U CN 203803293 U CN203803293 U CN 203803293U
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- China
- Prior art keywords
- steam
- compression
- pipe
- water
- separation device
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Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 46
- 238000000926 separation method Methods 0.000 title claims abstract description 16
- 230000006835 compression Effects 0.000 claims abstract description 70
- 238000007906 compression Methods 0.000 claims abstract description 70
- 235000014171 carbonated beverage Nutrition 0.000 claims description 13
- 238000001704 evaporation Methods 0.000 abstract description 7
- 230000008020 evaporation Effects 0.000 abstract description 7
- 239000012153 distilled water Substances 0.000 abstract description 6
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract 2
- 239000002994 raw material Substances 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 19
- 238000010438 heat treatment Methods 0.000 description 8
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 238000007701 flash-distillation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000009835 boiling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a steam-water pressurizing separation device. The steam-water pressurizing separation device comprises a compression cabin, a compression air cylinder, a steam input pipe, a steam output pipe and a water phase discharging pipe, wherein a piston rod free end of the compression air cylinder is provided with a compression piston; the compression piston is matched with the compression cabin; the steam input pipe, the steam output pipe and the water phase discharging pipe are all communicated with the compression cabin; the steam input pipe is provided with a first one-way valve; the steam output pipe is provided with a pressure control valve and a second one-way valve. The steam-water pressurizing separation device disclosed by the utility model can be used for pressurizing second-effect steam in a first-effect evaporator and separating a water phase in the steam; the pressurized second-effect steam can be introduced into a second-effect evaporator to heat a solution or raw material water needing to be concentrated so that heat energy is utilized sufficiently, and the energy consumption of solution evaporation and concentration and distilled water production is reduced.
Description
Technical field
The utility model relates to a kind of carbonated drink separation device, belongs to solution evaporation and concentration and distilled water production technical field.
Background technology
In solution evaporation and concentration and distilled water production, conventionally heat and need concentrated solution or raw water with an effect steam, imitate steam with needing concentrated solution or raw water to carry out condensation one simultaneously, the two effect steam that produce by an effect Steam Heating are used further to heat material solution or the raw water in 2nd effect evaporator, thereby make full use of heat energy, reduce the energy consumption that solution evaporation and concentration and distilled water are produced.But the deficiency of above-mentioned technique is, heating steam need to be kept apart by tube side and shell side with needing concentrated solution or raw water, avoids water solution or the raw water concentrated with needs that heating steam condensation forms to mix.Under normal circumstances, need concentrated solution or raw water to enter tube side by pipeline by 1st effective evaporator top and be distributed in each tubulation, make it evaporation thereby pass into concentrated solution or the raw water of needs that Boiler Steam calorifies in tube side in shell side.But due to the limited amount of tubulation, therefore in the solution in tubulation or raw water and shell side, the heat exchange of heating steam one side is insufficient, and heat exchanger time is long on the other hand, thereby has limited the raising of evaporator operation efficiency and performance.
In order to overcome the problems referred to above, heating steam can be carried out to pressurized treatments, again solution concentrated needs or raw water are preheated to boiling, under the effect of pressure-reducing valve, there is flash distillation effect in the heating steam that then makes to enter in evaporimeter, solution concentrated needs or raw water directly can be mixed with heating steam so on the one hand, can overcome on the other hand the problem that a large amount of condensations of heating steam the solution concentrated with needs or raw water mix.
Utility model content
The utility model is just for the needs of technical scheme described in background technology second segment, a kind of carbonated drink separation device is provided, in 1st effective evaporator two effect steam can be pressurizeed and separates water wherein, can pass in 2nd effect evaporator the concentrated solution of needs or raw water are heated through two effect steam of pressurization, thereby make full use of heat energy, reduce the energy consumption that solution evaporation and concentration and distilled water are produced.
For addressing the above problem, technical solution adopted in the utility model is as follows:
A kind of carbonated drink separation device, comprise: compression bin, compression cylinder, steam input pipe, steam output pipe, water discharge pipe, the piston rod free end of described compression cylinder is provided with compression piston, described compression piston coordinates with described compression bin, described steam input pipe, described steam output pipe and described water discharge pipe are all communicated with described compression bin, on described steam input pipe, be provided with the first check valve, described steam output pipe is provided with pressure-control valve and the second check valve.
As the improvement of technique scheme, the reciprocating motion path of described compression piston and described compression bin are vertically to arrange, described water discharge pipe is communicated with the bottom of described compression bin and is positioned at the minimum point top of described compression piston motion, and described steam input pipe and described steam output pipe are communicated with the top of described compression bin and are positioned at the peak top of described compression piston motion.
Compared with prior art, implementation result of the present utility model is as follows for the utility model:
Carbonated drink separation device described in the utility model, in 1st effective evaporator two effect steam can be pressurizeed and separates water wherein, can pass in 2nd effect evaporator the concentrated solution of needs or raw water are heated through two effect steam of pressurization, thereby make full use of heat energy, reduce the energy consumption that solution evaporation and concentration and distilled water are produced; And carbonated drink separation device described in the utility model has simple structure, and carbonated drink separate mode is effective and rapid, the advantage of stable work in work.
Brief description of the drawings
Fig. 1 is carbonated drink separation apparatus structure schematic diagram described in the utility model;
Fig. 2 is carbonated drink separation device described in the utility model and evaporimeter syndeton schematic diagram.
Detailed description of the invention
Content of the present utility model is described below in conjunction with specific embodiments.
As depicted in figs. 1 and 2, be carbonated drink separation apparatus structure schematic diagram described in the utility model.Carbonated drink separation device described in the utility model, comprise: compression bin 1, compression cylinder 2, steam input pipe 3, steam output pipe 4, water discharge pipe 5, the piston rod free end of described compression cylinder 2 is provided with compression piston 6, described compression piston 6 coordinates with described compression bin 1, described steam input pipe 3, described steam output pipe 4 and described water discharge pipe 5 are all communicated with described compression bin 1, on described steam input pipe 3, be provided with the first check valve 7, described steam output pipe 4 is provided with pressure-control valve 8 and the second check valve 9.Particularly, the reciprocating motion path of described compression piston 6 and described compression bin 1 are vertically to arrange, described water discharge pipe 5 is communicated with the bottom of described compression bin 1 and is positioned at the minimum point top that described compression piston 6 moves, and described steam input pipe 3 and described steam output pipe 4 are communicated with the top of described compression bin 1 and are positioned at the peak top that described compression piston 6 moves.
When job initiation, compression piston 6 is positioned at peak, then under driving, compression cylinder 2 moves downward, volume in compression bin 1 increases gradually, thereby air pressure declines, and the second check valve 9 has been blocked the opposing steam flow in steam output pipe 4, and steam can only flow in compression bin 1 from steam input pipe 3, therefore steam input pipe 3 is for connecting the steam outlet 11 of 1st effective evaporator 10, and 4 of steam output pipes are for connecting the vapor inlet port 13 of 2nd effect evaporator 12.
When compression piston 6 moves to after minimum point, under driving, compression cylinder 2 starts to move upward, volume in compression bin 1 reduces gradually, thereby pressure rises, originally the pressure that connects 2nd effect evaporator 12 1 sides due to the second check valve 9 is greater than the pressure that connects compression bin 1 one sides, therefore the second check valve 9 is still being blocked steam output pipe 4, the gas of pressurization gradually in compression bin 1 cannot be discharged from steam output pipe 4, and due to the effect of the first check valve 7, the gas of pressurization gradually in compression bin 1 also cannot be discharged from steam input pipe 3, in addition, along with the rising of compression piston 6, water discharge pipe 5 has been positioned at the below of compression piston 6, therefore compression bin 1 becomes airtight system, along with reducing of volume, air pressure strengthens gradually, part water recovery Cheng Shui, part water vapour forms high temperature and high pressure steam, in the time that the air pressure in air pressure and the 2nd effect evaporator 12 of compression bin 1 is close, because the pressure differential of pressure-control valve 8 both sides is less, therefore pressure-control valve 8 has still been blocked the admittance of steam output pipe 4, until being greater than the pressure differential of 2nd effect evaporator 12 and pressure-control valve 8 both sides, the air pressure of compression bin 1 reaches critical value, pressure-control valve 8 is opened, high temperature and high pressure steam in compression bin 1 enters 2nd effect evaporator 12, thereby form flash distillation effect.
When compression piston 6 moves to after peak, under driving, compression cylinder 2 starts to move downward, and the steam in 1st effective evaporator 10 flows in compression bin 1 from steam input pipe 3; In the time that compression piston 6 moves to minimum point, because water discharge pipe 5 is communicated with the bottom of described compression bin 1 and is positioned at the minimum point top that described compression piston 6 moves, now water discharge pipe 5 is communicated with the bottom of compression bin 1, the water of compression bin 1 interior condensation is discharged by water discharge pipe 5, then repeats above-mentioned circulation.
Above content is the detailed description of in conjunction with specific embodiments the utility model being done, and can not assert that the concrete enforcement of the utility model only limits to these explanations.For the utility model person of ordinary skill in the field, without departing from the concept of the premise utility, can also make some simple deduction or replace, all should be considered as belonging to the scope of the utility model protection.
Claims (2)
1. a carbonated drink separation device, it is characterized in that, comprise: compression bin (1), compression cylinder (2), steam input pipe (3), steam output pipe (4), water discharge pipe (5), the piston rod free end of described compression cylinder (2) is provided with compression piston (6), described compression piston (6) coordinates with described compression bin (1), described steam input pipe (3), described steam output pipe (4) and described water discharge pipe (5) are all communicated with described compression bin (1), on described steam input pipe (3), be provided with the first check valve (7), described steam output pipe (4) is provided with pressure-control valve (8) and the second check valve (9).
2. carbonated drink separation device as claimed in claim 1, it is characterized in that, the reciprocating motion path of described compression piston (6) and described compression bin (1) are vertically to arrange, described water discharge pipe (5) is communicated with the bottom of described compression bin (1) and is positioned at the minimum point top of described compression piston (6) motion, and described steam input pipe (3) and described steam output pipe (4) are communicated with the top of described compression bin (1) and are positioned at the peak top of described compression piston (6) motion.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420168879.6U CN203803293U (en) | 2014-04-09 | 2014-04-09 | Steam-water pressurizing separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420168879.6U CN203803293U (en) | 2014-04-09 | 2014-04-09 | Steam-water pressurizing separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203803293U true CN203803293U (en) | 2014-09-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420168879.6U Expired - Fee Related CN203803293U (en) | 2014-04-09 | 2014-04-09 | Steam-water pressurizing separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203803293U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107328250A (en) * | 2017-08-28 | 2017-11-07 | 贾海亮 | A kind of efficient heavy wash oil condensing unit |
| CN119120104A (en) * | 2024-10-09 | 2024-12-13 | 青岛金牛油脂科技有限公司 | A temperature-controlled circulating fatty acid extraction device |
-
2014
- 2014-04-09 CN CN201420168879.6U patent/CN203803293U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107328250A (en) * | 2017-08-28 | 2017-11-07 | 贾海亮 | A kind of efficient heavy wash oil condensing unit |
| CN119120104A (en) * | 2024-10-09 | 2024-12-13 | 青岛金牛油脂科技有限公司 | A temperature-controlled circulating fatty acid extraction device |
| CN119120104B (en) * | 2024-10-09 | 2025-04-18 | 青岛金牛油脂科技有限公司 | A temperature-controlled circulating fatty acid extraction device |
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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: 20140903 Termination date: 20210409 |
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| CF01 | Termination of patent right due to non-payment of annual fee |