CN204710071U - A kind of saturated vapor treatment system - Google Patents
A kind of saturated vapor treatment system Download PDFInfo
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- CN204710071U CN204710071U CN201520287724.9U CN201520287724U CN204710071U CN 204710071 U CN204710071 U CN 204710071U CN 201520287724 U CN201520287724 U CN 201520287724U CN 204710071 U CN204710071 U CN 204710071U
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- stop valve
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Abstract
The utility model relates to a kind of saturated vapor treatment system, comprise steam pre-treatment device, water separator, decompressor, steam trap connection A, steam trap connection B, intake-discharge pipe road A, intake-discharge pipe road B and saturated vapor part flow arrangement, steam pre-treatment device bottom is connected with steam trap connection A, 3. top be connected with water separator through stop valve, the bottom of water separator is connected with steam trap connection B, top is connected with the side of decompressor with Pressure gauge B through filter, the opposite side of decompressor is connected with steam diversion device, steam trap connection A is connected with intake-discharge pipe road A, steam trap connection B is connected with intake-discharge pipe road B.The utility model thoroughly solves the problem that water from steam divides higher, temperature not increase, and energy consumption have dropped 20%, and product quality is greatly improved.
Description
Technical field
The utility model relates to a kind of saturated vapor treatment system, belongs to steam treatment field.
Background technology
When liquid evaporates in limited confined space, fluid molecule enters upper space by liquid level, becomes steam molecule.Because steam molecule is among disorderly warm-up movement, they collide mutually, and and chamber wall and liquid level collide, when colliding with liquid level, some molecules then attract by fluid molecule, and return in liquid and become fluid molecule.When starting to evaporate, the molecule amount entering space is more than the number returning liquid Middle molecule, and along with proceeding of evaporation, the density of headspace vapor molecule constantly increases, and the molecule amount thus returned in liquid also increases.When the molecule amount entering space in the unit interval is equal with the molecule amount returned in liquid, then evaporation and condensation is in dynamic equilibrium state, although at this moment evaporation and condensation are still being carried out, in space, the density of steam molecule is no longer increasing, and state is now called saturation state.Liquid is in the saturated condition called saturated liquid, and the steam of its correspondence is saturated vapor, but is wet saturated steam at first, after the moisture in steam evaporates completely, be only dry saturated steam.Steam is never saturated to and wetly saturatedly arrives dry saturated process temperature again and do not increase, dry saturated after continue to heat, temperature can rise, and becomes superheated steam.
When the pressure of steam increases, the ability of water entrained by steam strengthens.Pressure is high, and molecular thermalmotion is strengthened, and kinetic energy strengthens, and water droplet is fractured into subparticle and is easily pulled away, and carbonated drink density contrast relation is little simultaneously, and separation difficulty, these all make water entrained by steam ability strengthen.
Summary of the invention
The purpose of this utility model is to provide a kind of saturated vapor treatment system, and the utility model thoroughly solves the problem that water from steam divides higher, temperature not increase, and energy consumption have dropped 20%, and product quality is greatly improved.The technical solution of the utility model is as follows:
A kind of saturated vapor treatment system, comprise steam pre-treatment device, water separator, decompressor, steam trap connection A, steam trap connection B, intake-discharge pipe road A, intake-discharge pipe road B and saturated vapor part flow arrangement, steam pre-treatment device bottom is connected with steam trap connection A, 3. top be connected with water separator through stop valve, the bottom of water separator is connected with steam trap connection B, top is connected with the side of decompressor with Pressure gauge B through filter, the opposite side of decompressor is connected with steam diversion device, steam trap connection A is connected with intake-discharge pipe road A, steam trap connection B is connected with intake-discharge pipe road B.
Described steam pre-treatment device comprises large gas bag, air wrap be provided with safety valve, stop valve 1., stop valve 2., stop valve 3. with Pressure gauge A; The effect of safety valve: when rated pressure is more than 10Mpa, safety valve action, starts pressure release, protects large gas bag normally can run in substitute pressure.
Baffle plate is provided with in described water separator; Described baffle plate is downward-sloping, is 75 degree with the angle of water separator inwall; Establish the baffle plate that is of five storeys in described water separator, baffle plate is the carbon steel sheet of 4mm thickness.
In existing technology, baffle plate is not had in water separator, when steam enters separator, along with the molecular kinetic energy of high pressure, high-speed motion increases severely, hydrone inside steam directly brings equipment into along with the air motion of the steam of high-speed cruising, cause the job insecurity of post facility, only change steam traffic direction, slow down the speed of service of steam, then by the principle of centrifugal force, allow moisture molecule be separated with steam, form saturated vapor, there is provided the saturated vapor of high-quality to like this rear class equipment, can production performance be improved, and the stabilization of product quality.
Described decompressor comprise stop valve 10., stop valve
, stop valve
, pressure-reducing valve and Pressure gauge C, wherein 10. stop valve is connected with pressure-reducing valve, pressure-reducing valve and stop valve
be connected, stop valve
be connected with Pressure gauge C, and stop valve 10., stop valve
, pressure-reducing valve and Pressure gauge C place pipeline and stop valve
place pipeline is in parallel.
Described steam trap connection A comprise stop valve 4., stop valve 5., stop valve 6., filter B and drain valve A, wherein, 4. stop valve is connected with filter B, filter B is connected with drain valve A, 5. drain valve A is connected with stop valve, and stop valve 4., stop valve 5., 6. place pipeline is in parallel with stop valve for filter B and drain valve A place pipeline.
Described steam trap connection B comprise stop valve 7., stop valve 8., stop valve 9. with drain valve B, wherein, 7. stop valve is connected with drain valve B, and 8. drain valve B is connected with stop valve, and stop valve 7., 8. 9. place pipeline is in parallel with stop valve with drain valve B place pipeline for stop valve.
Described saturated vapor part flow arrangement comprises sub-cylinder, stop valve
, stop valve
, enter quality-adjusting device A and enter quality-adjusting device B, wherein, sub-cylinder passes through stop valve
with enter quality-adjusting device A and be connected, sub-cylinder passes through stop valve
with enter quality-adjusting device B and be connected.
Utilize the utility model process saturated vapor technique as follows:
1. steam enter large gas bag by stop valve, rated pressure is 10Mpa, first close stop valve 4. with stop valve 5., open stop valve 6., condensed water is discharged by intake-discharge pipe road A, when large gas bag temperature rises to close to vapor (steam) temperature, close stop valve 6., open stop valve 4. with stop valve 5., drain valve A automatic operation, condensed water is discharged automatically by drain valve A; After air bag normal operation, open stop valve 3., steam enters water separator, due to the relation of the temperature difference, water separator can produce a large amount of condensed waters, therefore, first close stop valve 7. with stop valve 8., open stop valve 9., condensed water is discharged by pipeline B, when the temperature in water separator is close to vapor (steam) temperature, closes stop valve 9., open stop valve 7. with stop valve 8., condensed water by dredge valve B automatically discharge; When steam enters water separator, interior panelling can change the traffic direction of steam, reduce the speed of service, condensed water is allowed to be separated with steam by the effect of centrifugal force, due to the relation of density, condensed water down runs, and is discharged by the pipeline B in steam trap connection, steam up runs, and defines saturated vapor; 10. and stop valve saturated vapor entered filter and entered decompressor, and it is 2Mpa that Pressure gauge B shows pressure, during adjustment pressure, closed stop valve
, open stop valve
, after 30 seconds, close stop valve
10. and stop valve, open stop valve
, making Pressure gauge B show pressure is 2Mpa; Saturated vapor enters saturated vapor part flow arrangement after decompressor, and saturated vapor is by entering quality-adjusting device A and enter quality-adjusting device B to flow out.
The utility model compared with prior art has the following advantages:
The utility model overcomes the problem that water from steam in prior art divides content, in prior art, steam moisture is larger, easily have a negative impact during use, as: moisture is too high, temperature does not increase, starch curing degree only maintains between 20-30, efficiency decline, energy consumption rising etc.And the utility model thoroughly solves moisture is higher, temperature does not increase problem, energy consumption have dropped 20%, and product quality have also been obtained very large lifting (the mainly slaking of starch, curing degree reaches more than 70-75).
Accompanying drawing explanation
Fig. 1 is the utility model saturated vapor treatment system figure;
Fig. 2 is water separator figure.
Symbol description:
1. steam pre-treatment device, 2. water separator, 3. decompressor, 4. steam trap connection A, 5. steam trap connection B, 6. intake-discharge pipe road A, 7. intake-discharge pipe road B, 8. saturated vapor part flow arrangement, 9. filter, 10. Pressure gauge B, 11. large gas bags, 12. safety valves, 13. stop valves 1., 14. stop valves 2., 15. stop valves 3., 16. Pressure gauge A, 21. baffle plates, 31. stop valves 10., 32. stop valves
, 33. stop valves
, 34. pressure-reducing valves, 35. Pressure gauge C, 41. stop valves 4., 42. stop valves 5., 43. stop valves 6., 44. filter B, 45. drain valve A, 51. stop valves 7., 52. stop valves 8., 53. stop valves 9., 54. drain valve B, 81. sub-cylinders, 82. stop valves
, 83. stop valves
, 84. enter quality-adjusting device A, 85. and enter quality-adjusting device B.
Detailed description of the invention
Further describe the utility model below in conjunction with specific embodiment, advantage and disadvantage of the present utility model will be more clear along with description.But embodiment is only exemplary, does not form any restriction to scope of the present utility model.It will be understood by those skilled in the art that and do not departing under spirit and scope of the present utility model and can modify to the details of technical solutions of the utility model and form or replace, but these amendments and replacement all fall in protection domain of the present utility model.
Embodiment 1 one kinds of saturated vapor treatment systems
As depicted in figs. 1 and 2, described saturated vapor treatment system comprises steam pre-treatment device 1, water separator 2, decompressor 3, steam trap connection A 4, steam trap connection B 5, intake-discharge pipe road A 6, intake-discharge pipe road B 7 and saturated vapor part flow arrangement 8, steam pre-treatment device 1 bottom is connected with steam trap connection A 4, 3. top 14 to be connected with water separator 2 through stop valve, the bottom of water separator 2 is connected with steam trap connection B 5, top is connected with the side of decompressor 3 with Pressure gauge B 10 through filter 9, the opposite side of decompressor 3 is connected with steam diversion device 8, steam trap connection A 4 is connected with intake-discharge pipe road A 6, steam trap connection B 5 is connected with intake-discharge pipe road B 7,
Described steam pre-treatment device 1 comprises large gas bag 11, large gas bag 11 be provided with safety valve 12, stop valve 1. 13, stop valve 2. 14, stop valve 3. 15 and Pressure gauge A16;
Baffle plate 21 is provided with in described water separator 2; Described baffle plate 21 is downward-sloping, is 75 degree with the angle of water separator 2 inwall; Establish the baffle plate 21 that is of five storeys in described water separator 2, baffle plate 21 is the carbon steel sheet of 4mm thickness;
Described decompressor 3 comprise stop valve 10. 31, stop valve
32, stop valve
33, pressure-reducing valve 34 and Pressure gauge C 35, wherein 10. stop valve 31 to be connected with pressure-reducing valve 34, pressure-reducing valve 34 and stop valve
32 are connected, stop valve
32 are connected with Pressure gauge C35, and stop valve 10. 31, stop valve
32, pressure-reducing valve 34 and Pressure gauge C 35 place pipeline and stop valve
33 place pipelines are in parallel;
Described steam trap connection A 4 comprise stop valve 4. 41, stop valve 5. 42, stop valve 6. 43, filter B 44 and drain valve A 45, wherein, 4. stop valve 41 to be connected with filter B 44, filter B 44 is connected with drain valve A45,5. drain valve A45 and stop valve 42 to be connected, and stop valve 4. 41, stop valve 5. 42,6. 43 place pipelines are in parallel with stop valve for filter B 44 and drain valve A45 place pipeline;
Described steam trap connection B 5 comprise stop valve 7. 51, stop valve 8. 52, stop valve 9. 53 and drain valve B54, wherein, 7. stop valve 51 to be connected with drain valve B54,8. drain valve B54 and stop valve 52 to be connected, and stop valve 7. 51, stop valve 8. 52 and drain valve B54 place pipeline 9. 53 place pipelines are in parallel with stop valve;
Described saturated vapor part flow arrangement 8 comprises sub-cylinder 81, stop valve
82, stop valve
83, enter quality-adjusting device A84 and enter quality-adjusting device B85, wherein, sub-cylinder 81 passes through stop valve
82 with enter quality-adjusting device A84 and be connected, sub-cylinder 81 passes through stop valve
83 with enter quality-adjusting device B85 and be connected.
Embodiment 2
On the basis of embodiment 1, as depicted in figs. 1 and 2, saturated vapor processing procedure is as follows:
1. steam 13 enter large gas bag 11 by stop valve, rated pressure is 10Mpa, first stop valve 4. 41 and stop valve 5. 42 is closed, open stop valve 6. 43, condensed water is discharged by intake-discharge pipe road A6, when large gas bag 11 temperature rises to close to vapor (steam) temperature, close stop valve 6. 43, open stop valve 4. 41 and stop valve 5. 42, drain valve A45 automatic operations, condensed water is discharged automatically by drain valve A45; After large gas bag 11 normal operation, open stop valve 3. 15, steam enters water separator 2, due to the relation of the temperature difference, water separator 2 can produce a large amount of condensed waters, therefore, first closes stop valve 7. 51 and stop valve 8. 52, open stop valve 9. 53, condensed water is discharged by pipeline B 7, when the temperature in water separator 2 is close to vapor (steam) temperature, closes stop valve 9. 53, open stop valve 7. 51 and stop valve 8. 52, condensed water is discharged automatically by dredging valve B7; When steam enters water separator 2, interior panelling 21 can change the traffic direction of steam, and reduce the speed of service, condensed water down runs, and enter in steam trap connection B5, steam up runs, and defines saturated vapor; Saturated vapor entered filter 9 and entered decompressor 3, and it is 2Mpa that Pressure gauge B10 shows pressure, during adjustment pressure, closed stop valve 10. 31 and stop valve
32, open stop valve
after 33,30 seconds, close stop valve
33, open stop valve 10. 31 and stop valve
32, making Pressure gauge B10 show pressure is 2Mpa; Saturated vapor enters saturated vapor part flow arrangement 8 after decompressor 3, and saturated vapor is by entering quality-adjusting device A84 and enter quality-adjusting device B85 to flow out.
Claims (8)
1. a saturated vapor treatment system, it is characterized in that, comprise steam pre-treatment device, water separator, decompressor, steam trap connection A, steam trap connection B, intake-discharge pipe road A, intake-discharge pipe road B and saturated vapor part flow arrangement, steam pre-treatment device bottom is connected with steam trap connection A, 3. top be connected with water separator through stop valve, the bottom of water separator is connected with steam trap connection B, top is connected with the side of decompressor with Pressure gauge B through filter, the opposite side of decompressor is connected with steam diversion device, steam trap connection A is connected with intake-discharge pipe road A, steam trap connection B is connected with intake-discharge pipe road B.
2. saturated vapor treatment system according to claim 1, is characterized in that, described steam pre-treatment device comprises large gas bag, air wrap be provided with safety valve, stop valve 1., stop valve 2., stop valve 3. with Pressure gauge A.
3. saturated vapor treatment system according to claim 1, is characterized in that, is provided with baffle plate in described water separator.
4. saturated vapor treatment system according to claim 3, is characterized in that, described baffle plate is downward-sloping, is 75 degree with the angle of water separator inwall; Establish the baffle plate that is of five storeys in described water separator, baffle plate is the carbon steel sheet of 4mm thickness.
5. saturated vapor treatment system according to claim 1, is characterized in that, described decompressor comprise stop valve 10., stop valve
stop valve
pressure-reducing valve and Pressure gauge C, wherein 10. stop valve is connected with pressure-reducing valve, pressure-reducing valve and stop valve
be connected, stop valve
be connected with Pressure gauge C, and stop valve 10., stop valve
pressure-reducing valve and Pressure gauge C place pipeline and stop valve
place pipeline is in parallel.
6. saturated vapor treatment system according to claim 1, it is characterized in that, described steam trap connection A comprise stop valve 4., stop valve 5., stop valve 6., filter B and drain valve A, wherein, 4. stop valve is connected with filter B, filter B is connected with drain valve A, and 5. drain valve A is connected with stop valve, and stop valve 4., stop valve 5., 6. place pipeline is in parallel with stop valve for filter B and drain valve A place pipeline.
7. saturated vapor treatment system according to claim 1, it is characterized in that, described steam trap connection B comprise stop valve 7., stop valve 8., stop valve 9. with drain valve B, wherein, 7. stop valve is connected with drain valve B, 8. drain valve B is connected with stop valve, and stop valve 7., 8. 9. place pipeline is in parallel with stop valve with drain valve B place pipeline for stop valve.
8. saturated vapor treatment system according to claim 1, is characterized in that, described saturated vapor part flow arrangement comprises sub-cylinder, stop valve
stop valve
enter quality-adjusting device A and enter quality-adjusting device B, wherein, sub-cylinder passes through stop valve
with enter quality-adjusting device A and be connected, sub-cylinder passes through stop valve
with enter quality-adjusting device B and be connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520287724.9U CN204710071U (en) | 2015-05-06 | 2015-05-06 | A kind of saturated vapor treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520287724.9U CN204710071U (en) | 2015-05-06 | 2015-05-06 | A kind of saturated vapor treatment system |
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| Publication Number | Publication Date |
|---|---|
| CN204710071U true CN204710071U (en) | 2015-10-21 |
Family
ID=54309102
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|---|---|---|---|
| CN201520287724.9U Active CN204710071U (en) | 2015-05-06 | 2015-05-06 | A kind of saturated vapor treatment system |
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| Country | Link |
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| CN (1) | CN204710071U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108105869A (en) * | 2017-12-21 | 2018-06-01 | 洛阳沃辉机械有限公司 | A kind of air purifier and air purification method |
| CN108355445A (en) * | 2018-03-20 | 2018-08-03 | 中节能(宿迁)生物质能发电有限公司 | A kind of jet chimney water separator |
-
2015
- 2015-05-06 CN CN201520287724.9U patent/CN204710071U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108105869A (en) * | 2017-12-21 | 2018-06-01 | 洛阳沃辉机械有限公司 | A kind of air purifier and air purification method |
| CN108355445A (en) * | 2018-03-20 | 2018-08-03 | 中节能(宿迁)生物质能发电有限公司 | A kind of jet chimney water separator |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220505 Address after: 062650 north of wangweitun village, Machang Town, Qing County, Cangzhou City, Hebei Province Patentee after: Hebei helimei Biotechnology Co.,Ltd. Address before: A516, kaichi building, No.2 Jinfu Road, Daxing District Economic Development Zone, Beijing 102600 Patentee before: BEIJING HELIOMY BIOLOGICAL TECHNOLOGY Co.,Ltd. |