CN203309504U - Air-separation steam trap device - Google Patents
Air-separation steam trap device Download PDFInfo
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- CN203309504U CN203309504U CN2013203266192U CN201320326619U CN203309504U CN 203309504 U CN203309504 U CN 203309504U CN 2013203266192 U CN2013203266192 U CN 2013203266192U CN 201320326619 U CN201320326619 U CN 201320326619U CN 203309504 U CN203309504 U CN 203309504U
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- steam
- vapor
- pipeline
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- separation
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Abstract
The utility model discloses an air-separation steam trap device. The air-separation steam trap device comprises a floating-ball type trap and a steam-liquid separator, wherein the floating-ball type trap is arranged on a steam outlet pipeline of a steam heat exchanger, and the steam outlet pipeline is also provided with a pressure gauge and a cut-off valve; the steam-liquid separator is buried under the ground and is connected with the floating-ball type trap by a pipeline; an outlet of the steam-liquid separator is provided with a discharging pipeline which is used for discharging cooling water into a recovery device and a steam-liquid separation pipeline which is connected with the discharging pipeline and is used for emptying hot air upwards. The air-separation steam trap device disclosed by the utility model solves the problems of large steam consumption, unsmooth water drainage, frequent maintenance and the like in an existing air-separation purifying device and has the characteristics of low operating cost, simplicity and convenience in maintenance and the like.
Description
Technical field
The utility model belongs to air purification field, is specifically related to a kind of sky and divides steam drainage device.
Background technique
An empty minute purification plant is the empty minute indispensable preposition equipment of low temperature separation unit.The impurity such as airborne water, carbon dioxide are removed in molecular sieve system.After molecular sieve adsorption, must after regeneration, just can recycle.And the essential condition that high temperature is regenerating molecular sieve is heated and generally with low pressure steam, is carried out in heat exchanger regeneration gas at present.Can effectively steam condensate is separated and discharge fast be the requirement of cleaning system.
The domestic measure of taking at present is to add that with vapor heat exchanger vapor-liquid separation tank, level meter, diaphragm type STEAM TRAP, tube-cooled catch basin realize regeneration gas is heated.The shortcoming that adopts this method is that steam consumption quantity is large, and equipment all belongs to pressurized container and pressure piping, and the complex structure maintenance cost is high.
Foreign department minute producer is used electric heating and vapor heat exchanger jointly to complete regeneration gas is heated, shortcoming device structure complexity, and control is had relatively high expectations, and causes the raising of empty minute operation cost.
Summary of the invention
The purpose of this utility model is to provide a kind of sky to divide steam drainage device, and the problem such as solved that existing sky divides that the purification plant steam consumption quantity is large, blocked drain, maintenance are frequent has the characteristics such as low operating cost, convenience easy to maintenance.
For achieving the above object, the technical solution of the utility model is:
A kind of sky divides steam drainage device, and it comprises, float type steam trap is arranged on the steam (vapor) outlet pipeline of vapor heat exchanger, also is provided with pressure gauge, cut-off valve on this steam (vapor) outlet pipeline; Vapor-liquid separator, be embedded in undergroundly, and it is connected in float type steam trap by pipeline, and the vapor-liquid separator outlet arranges a discharge cooling water and advances the upwards vapor-liquid separation pipeline of emptying hot gas of the blowdown piping of recovering device and be attached thereto.
Further, the emergent discharge pipe in steam (vapor) outlet pipeline Shang She mono-tunnel of described vapor heat exchanger and corresponding dump valve.
The utility model realizes that by float type steam trap the steam condensate in vapor heat exchanger is discharged into to underground vapor-liquid separator carries out that next step is cooling, in vapor-liquid separator and discharge pipe, again separate hot gas and enter atmosphere by the discharge pipe top, condensed water enters reclaim line.
The beneficial effects of the utility model:
The utility model divides the heat exchange steam trap connection normally to move at sky to have realized low-cost production, the unfavorable factor such as overcome that steam consumption quantity is large, blocked drain, maintenance are frequent.
The accompanying drawing explanation
Fig. 1 is the utility model one embodiment's structural representation.
Embodiment
Referring to Fig. 1, a kind of sky of the present utility model divides steam drainage device, and it comprises, float type steam trap 1 is arranged on the steam (vapor) outlet pipeline 101 of vapor heat exchanger 100, on this steam (vapor) outlet pipeline 101, also is provided with pressure gauge, cut-off valve 2; Vapor-liquid separator 3, be embedded in undergroundly, and it is connected in float type steam trap 1 by pipeline, and vapor-liquid separator 3 outlets arrange a discharge cooling water and advance the upwards vapor-liquid separation pipeline 5 of emptying hot gas of the blowdown piping 4 of recovering device 6 and be attached thereto.
Further, the emergent discharge pipe 7 in steam (vapor) outlet pipeline Shang She mono-tunnel of described vapor heat exchanger 100 and corresponding dump valve 8.
During heat exchanger work; by outlet regeneration gas temperature, judge the heat exchange situation and delivery gauge can judge vapor pressure; float type steam trap can effectively emit and not waste steam to the condensed water produced in time; change miscellaneous works such as needing in the past manual control and site disposal, guaranteed the heat exchanger efficient operation.
Claims (2)
1. a sky divides steam drainage device, it is characterized in that, comprise,
Float type steam trap, be arranged on the steam (vapor) outlet pipeline of vapor heat exchanger, also is provided with pressure gauge, cut-off valve on this steam (vapor) outlet pipeline;
Vapor-liquid separator, be embedded in undergroundly, and it is connected in float type steam trap by pipeline, and the vapor-liquid separator outlet arranges a discharge cooling water and advances the upwards vapor-liquid separation pipeline of emptying hot gas of the blowdown piping of recovering device and be attached thereto.
2. sky as claimed in claim 1 divides steam drainage device, it is characterized in that the emergent discharge pipe in steam (vapor) outlet pipeline Shang She mono-tunnel of described vapor heat exchanger and corresponding dump valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203266192U CN203309504U (en) | 2013-06-06 | 2013-06-06 | Air-separation steam trap device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203266192U CN203309504U (en) | 2013-06-06 | 2013-06-06 | Air-separation steam trap device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203309504U true CN203309504U (en) | 2013-11-27 |
Family
ID=49615713
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013203266192U Expired - Fee Related CN203309504U (en) | 2013-06-06 | 2013-06-06 | Air-separation steam trap device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203309504U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105090733A (en) * | 2015-09-06 | 2015-11-25 | 宜兴市昌吉利化工有限公司 | Automatic draining device adopting overflowing method |
| CN113586936A (en) * | 2021-06-29 | 2021-11-02 | 无锡新联热力有限公司 | Buried water-cooled steam pipeline drainage system |
-
2013
- 2013-06-06 CN CN2013203266192U patent/CN203309504U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105090733A (en) * | 2015-09-06 | 2015-11-25 | 宜兴市昌吉利化工有限公司 | Automatic draining device adopting overflowing method |
| CN113586936A (en) * | 2021-06-29 | 2021-11-02 | 无锡新联热力有限公司 | Buried water-cooled steam pipeline drainage system |
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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: 20131127 Termination date: 20180606 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |