CN202253580U - rotary film deaerator - Google Patents
rotary film deaerator Download PDFInfo
- Publication number
- CN202253580U CN202253580U CN2011203339141U CN201120333914U CN202253580U CN 202253580 U CN202253580 U CN 202253580U CN 2011203339141 U CN2011203339141 U CN 2011203339141U CN 201120333914 U CN201120333914 U CN 201120333914U CN 202253580 U CN202253580 U CN 202253580U
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- China
- Prior art keywords
- pipe
- water
- steam
- oxygen
- eddy flow
- 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.)
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 53
- 235000014171 carbonated beverage Nutrition 0.000 claims description 11
- 125000006850 spacer group Chemical group 0.000 claims description 11
- 239000000945 filler Substances 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000012528 membrane Substances 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 claims description 2
- 238000003466 welding Methods 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 5
- 229910052760 oxygen Inorganic materials 0.000 abstract description 5
- 239000001301 oxygen Substances 0.000 abstract description 5
- 238000000926 separation method Methods 0.000 abstract description 3
- 238000005192 partition Methods 0.000 abstract 3
- 239000007921 spray Substances 0.000 abstract 2
- 238000012856 packing Methods 0.000 abstract 1
- 238000006392 deoxygenation reaction Methods 0.000 description 16
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
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- Physical Water Treatments (AREA)
- Degasification And Air Bubble Elimination (AREA)
Abstract
The utility model relates to a rotary film deaerator. The device comprises a deaerating tower and a water tank, wherein a water chamber and an auxiliary steam chamber which are composed of a rotational flow spray pipe, a downcomer, an upper partition plate, a middle partition plate and a lower partition plate are arranged at the upper part of the deaerating tower, one side of the water chamber is connected with a water supply inlet mixing pipe, one side of the auxiliary steam chamber is connected with an auxiliary steam pipe, a steam-water separation device and an exhaust pipe are arranged at the top of the deaerating tower, a steam-water free exchange space is arranged below the rotational flow spray pipe, a trickle secondary distributor and a packing set are arranged below the steam-water free exchange space, four sets of steam lifting caps are arranged at the bottom of the deaerating tower, a water falling pipe is arranged in the middle of the deaerating tower, the steam. The utility model discloses make the dissolved oxygen volume of deoxidization aquatic remain throughout below 7 mug/L, strong adaptability, the running noise is little, and energy-conserving effect is showing.
Description
Technical field
The utility model relates to the improvement of the used deaerating plants of all kinds of power plant such as a kind of thermal power plant, garbage incinerating power plant.Be a kind of membrane deaerator efficiently specifically.
Background technology
The deoxygenation of boiler feedwater is a crucial link in power plant, and existing oxygen-eliminating device mainly contains upright tower from the appearance, water tank two parts are formed.The shortcoming of these deaerating plants mainly is a complex structure, the operation noise is big, deaerating effect is unstable, can not guarantee the standard-required of boiler feedwater fully.
Summary of the invention
The purpose of the utility model is to overcome the shortcoming in the above-mentioned technology, a kind of architecture advances is proposed membrane deaerator, make that dissolved oxygen amount maintains below the 7 μ g/L all the time in the deaerated water, adaptability is strong, the operation noise is little, energy-saving effect is remarkable.
The purpose of the utility model is realized by following technical scheme: this membrane deaerator comprises oxygen-removing tower and water tank two parts; The hydroecium and the auxiliary steam chest of eddy flow jet pipe and downspout and upper spacer, median septum, lower clapboard composition are housed on the top of oxygen-removing tower; One side of hydroecium connects feed-water intake and mixes pipe, and a side of auxiliary steam chest connects air vent pipework, at the top of oxygen-removing tower water separator and blast pipe is housed; Eddy flow jet pipe below is the free swapace of carbonated drink; Trickle secondary distribution device and filler group are equipped with in the below of the free swapace of carbonated drink, are equipped with four groups in the bottom of oxygen-removing tower and rise the vapour cap, and the centre is a downpipe; Steam Pipe, downpipe and assistant heating pipe are housed on water tank, and water tank adopts crowd's pipe to be connected with oxygen-removing tower.
Between upper spacer, median septum, lower clapboard downspout and eddy flow jet pipe in-line arrangement or wrong row in proportion; And welding is fixing; Form the hydroecium on top and the auxiliary steam chest of bottom respectively, be distributed with the micropore by the rule discharging on the eddy flow jet pipe, the upper end of downspout is processed with the dirty otch of liquid.
The deoxygenation and the heat and mass transfer process of boiler feedwater are accomplished in oxygen-removing tower, the deoxygenation in feedwater following two stages of process:
Phase I, water mixes in eddy flow jet pipe, downspout and upper spacer that pipe gets into oxygen-removing tower top, the hydroecium that median septum is formed, through descending along the inwall eddy flow in the entering of the micropore on the eddy flow jet pipe eddy flow jet pipe from feed-water intake.The steam that rises gets into the eddy flow jet pipe from the bottom of eddy flow jet pipe; With the moisture film of ejection carry out after the heat and mass condensation with the eddy flow jet pipe in moisture film together flow downward; Water flow out behind the eddy flow jet pipe the free swapace of carbonated drink continue with the steam heat and mass that rises until falling into trickle secondary distribution device, redistribute the second time of accomplishing phase I deoxygenation and trickle.Incondensable gases such as the oxygen that is separated, carbon dioxide enter atmosphere through the water separator separation; Water is prevented from falling on the upper spacer; Otch through downspout flows down; Continue above-mentioned heat and mass transfer process with the steam that rises, reach the purpose of deoxygenation, also prevented the water that upper spacer is possible simultaneously.Second stage, feedwater get into filler after falling into trickle secondary distribution device, have further increased the carbonated drink contact area, accomplish the second stage deoxygenation.Steam gets into rising in the vapour cap the tower from the water tank Steam Pipe, gets into oxygen-removing tower through four groups of secondary distribution that rise the vapour cap, and the water heat exchange that elder generation and filler group are come is accomplished the second stage deoxygenation after trickle secondary distribution device gets into the free swapace of carbonated drink.It is subsequent use that water after the deoxygenation gets into water tank through downpipe.
When feedwater load change amplitude surpasses declared working condition, launch air vent pipework, make steam get into the auxiliary steam chest of median septum and lower clapboard composition; Micropore through the eddy flow jet pipe is the additional rotary power of feedwater under the eddy flow; Heat simultaneously, promote deoxygenation, thereby guarantee deaerating effect.
When the feed temperature in the water tank is on the low side, launch the assistant heating pipe, steam is got in the water in the water tank, carry out assistant heating, to keep normal water temperature, guarantee deaerating effect.
The utility model has the advantages that adaptability is strong, the operation noise is little, and energy-saving effect is remarkable, and the deaerated water dissolved oxygen amount is maintained below the 7 μ g/L all the time.
Description of drawings
Below in conjunction with accompanying drawing and embodiment the utility model is further specified.
Fig. 1 is the generalized section of oxygen-removing tower;
Fig. 2 is the generalized section of deoxygenation water tank.
In Fig. 1: 1. oxygen-removing tower; 2. feed-water intake mixes pipe; 3. water separator; 4. blast pipe; 5. eddy flow jet pipe; 6. downspout; 7. upper spacer; 8. hydroecium; 9. median septum; 10. auxiliary steam chest; 11. air vent pipework; 12. lower clapboard; 13. the free swapace of carbonated drink; 14. trickle secondary distribution device; 15. filler group; 16. rise the vapour cap; 17. downpipe.
In Fig. 2: 18. water tanks; 19. Steam Pipe; 20. assistant heating pipe.
The specific embodiment
Feedwater is mixed in the hydroecium 8 that eddy flow jet pipe 5 that pipe 2 gets into oxygen-removing towers 1 top, downspout 6 and upper spacer 7, median septum 9 form by feed-water intake, descends along the inwall eddy flow through the entering of the micropore on the eddy flow jet pipe 5 eddy flow jet pipe 5 is interior.The steam that rises gets into eddy flow jet pipe 5 from the bottom of eddy flow jet pipe 5; After carrying out the heat and mass condensation with the moisture film of eddy flow jet pipe 5 ejection; Together flow downward; Water flow out eddy flow jet pipe 5 backs the free swapace 13 of carbonated drink continue with the steam heat and mass that rises until falling into trickle secondary distribution device 14, accomplish phase I deoxygenation and trickle secondary and redistribute.Incondensable gases such as the oxygen that is separated, carbon dioxide enter atmosphere through water separator 3 separation through blast pipe 4; Water is prevented from falling on the upper spacer 7; Otch through downspout 6 flows down; Continue above-mentioned heat and mass transfer process with the steam that rises, reach the purpose of deoxygenation, also prevented the water that upper spacer 7 is possible simultaneously.Feedwater falls into trickle secondary distribution device 14 backs and gets into filler group 15, has further increased the carbonated drink contact area, accomplishes the second stage deoxygenation.Water after the deoxygenation gets in the water tank 18 through downpipe 17 successively.The Steam Pipe 19 of steam from water tank 18 gets into rising in the vapour cap 16 oxygen-removing tower 1; Get in the oxygen-removing tower 1 through four groups of secondary distribution that rise vapour cap 16; Water heat exchange in elder generation and the filler group 15; After accomplishing the second stage deoxygenation, get into the free swapace 13 of carbonated drink, continue to carry out heat and mass with the water that flows down through trickle secondary distribution device 14.
When feedwater load change amplitude surpasses declared working condition; Launch air vent pipework 11; Making steam get into the auxiliary steam chest 10 of eddy flow jet pipe 5, downspout 6 and median septum 9, lower clapboard 12 compositions, is the additional rotary power of feedwater under the eddy flow through the micropore on the eddy flow jet pipe 5, heats simultaneously; Promote deoxygenation, thereby guarantee deaerating effect.
When the feed temperature in the water tank is on the low side, launch assistant heating pipe 20, steam is got in the water in the water tank 18, carry out assistant heating, to keep normal water temperature, guarantee deaerating effect.
Claims (2)
1. membrane deaerator; Comprise oxygen-removing tower (1) and water tank (16) two parts; It is characterized in that: hydroecium (8) and auxiliary steam chest (10) that eddy flow jet pipe (5) and downspout (6) and upper spacer (7), median septum (9), lower clapboard (12) composition are housed on the top of oxygen-removing tower (1); One side of hydroecium (8) connects feed-water intake and mixes pipe (2), and a side of auxiliary steam chest (10) connects air vent pipework (11), and water separator (3) and blast pipe (4) are housed at the top of oxygen-removing tower (1); Eddy flow jet pipe (5) below is the free swapace of carbonated drink (13); Trickle secondary distribution device (14) and filler group (15) are equipped with in the below of the free swapace of carbonated drink (13), are equipped with four groups in the bottom of oxygen-removing tower (1) and rise vapour cap (16), and the centre is downpipe (17); Steam Pipe (19), downpipe (17) and assistant heating pipe (20) are housed on water tank (18), and water tank (18) adopts crowd's pipe to be connected with oxygen-removing tower (1).
2. membrane deaerator according to claim 1; It is characterized in that: between upper spacer (7), median septum (9), lower clapboard (12) downspout (6) and eddy flow jet pipe (5) in-line arrangement or wrong row in proportion; And welding is fixing; Form the hydroecium (8) on top and the auxiliary steam chest (10) of bottom respectively, be distributed with the micropore by the rule discharging on the eddy flow jet pipe (5), the upper end of downspout (6) is processed with the dirty otch of liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203339141U CN202253580U (en) | 2011-09-07 | 2011-09-07 | rotary film deaerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203339141U CN202253580U (en) | 2011-09-07 | 2011-09-07 | rotary film deaerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202253580U true CN202253580U (en) | 2012-05-30 |
Family
ID=46114816
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203339141U Expired - Fee Related CN202253580U (en) | 2011-09-07 | 2011-09-07 | rotary film deaerator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202253580U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107076409A (en) * | 2014-07-24 | 2017-08-18 | 能源技术研究所科研和设计股份公司 | Degasser (variant) |
| CN117190163A (en) * | 2023-10-11 | 2023-12-08 | 山东华昱压力容器股份有限公司 | High-efficiency rotary film deaerator |
-
2011
- 2011-09-07 CN CN2011203339141U patent/CN202253580U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107076409A (en) * | 2014-07-24 | 2017-08-18 | 能源技术研究所科研和设计股份公司 | Degasser (variant) |
| CN107076409B (en) * | 2014-07-24 | 2019-03-05 | 能源技术研究所科研和设计股份公司 | Degasser (variant) |
| CN117190163A (en) * | 2023-10-11 | 2023-12-08 | 山东华昱压力容器股份有限公司 | High-efficiency rotary film deaerator |
| CN117190163B (en) * | 2023-10-11 | 2024-05-24 | 山东华昱压力容器股份有限公司 | High-efficiency rotary film deaerator |
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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: 20120530 Termination date: 20150907 |
|
| EXPY | Termination of patent right or utility model |