CN202700360U - Oxidation air spraying and sucking device used in desulfurizing absorption tower - Google Patents
Oxidation air spraying and sucking device used in desulfurizing absorption tower Download PDFInfo
- Publication number
- CN202700360U CN202700360U CN 201220361928 CN201220361928U CN202700360U CN 202700360 U CN202700360 U CN 202700360U CN 201220361928 CN201220361928 CN 201220361928 CN 201220361928 U CN201220361928 U CN 201220361928U CN 202700360 U CN202700360 U CN 202700360U
- Authority
- CN
- China
- Prior art keywords
- slurries
- aspiration channel
- oxidation
- dilatation
- air
- 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 - Lifetime
Links
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 106
- 230000003647 oxidation Effects 0.000 title claims abstract description 105
- 238000010521 absorption reaction Methods 0.000 title abstract description 9
- 230000003009 desulfurizing Effects 0.000 title abstract 2
- 238000005507 spraying Methods 0.000 title abstract 2
- 239000002002 slurry Substances 0.000 claims abstract description 114
- 239000007788 liquid Substances 0.000 claims abstract description 23
- 238000006477 desulfuration reaction Methods 0.000 claims description 16
- 239000007921 spray Substances 0.000 claims description 9
- 230000000694 effects Effects 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000005381 potential energy Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 230000001590 oxidative Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000009527 percussion Methods 0.000 description 1
- 230000000505 pernicious Effects 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 230000000630 rising Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Abstract
The utility model relates to an oxidation air spraying and sucking device used in a desulfurizing absorption tower. The device comprises a slurry accelerating pipe (1), a slurry expansion air sucking pipe (2), an air sucking pipe sleeve (3), an oxidation air-slurry mixing pipe (4) and an oxidation air sucking pipe (5); the air sucking pipe sleeve (3) is sleeved outside the slurry expansion air sucking pipe (2), the liquid outlet end of the slurry accelerating pipe (1) is axially connected with the liquid inlet end of the slurry expansion air sucking pipe (2) and one end of the air sucking pipe sleeve (3), and the other end of the air sucking pipe sleeve (3) is communicated with the liquid inlet end of the oxidation air-slurry mixing pipe (4); and one end of the oxidation air sucking pipe (5) is communicated with the air sucking pipe sleeve (3) in a horizontal direction. By the device, the oxidation air can be sucked quickly and is mixed with slurry; and the pressure requirement on oxidation air is low, the independence on an oxidation air blower is low, running cost can be saved, and noise can be reduced.
Description
Technical field
The utility model relates to smoke eliminator, is specifically related to the oxidation wind injection suction apparatus that a kind of desulfuration absorbing tower uses.
Background technology
In spray absorption tower when operation, is in order to make the SO that sucks slurries
2Be removed Deng pernicious gas, the oxidation air that need to utilize the equipment such as oxidation fan to provide is transported in the slurries of absorption tower, for slurries provide oxygen, with the SO in the slurries
2, H
2SO
3, SO
3 2-Deng being oxidized to SO
4 2-And with slurries in Ca
2+Reaction forms CaSO
42H
2O often claims on the engineering that oxidation air is oxidation wind.The tradition desulfuration absorbing tower need to arrange mechanical stirring device and oxidation air and slurries be filled part mixes in stock tank when passing into oxidation air to stock tank, with increase oxidation contact area, and quickening oxidation reaction speed.Existing oxidation air adding method is to send into the ad-hoc location of stock tank inside, absorption tower after utilizing oxidation fan that air is boosted, and this oxidation wind adding mode exists that energy consumption is high, noise is high and the reliability shortcoming that can't overcome such as low.
Summary of the invention
[0003] the purpose of this utility model provides and a kind ofly can suck fast oxidation air and oxidation air is mixed mutually with slurries fast, require desulfuration absorbing tower lower, lower to the dependence of oxidation fan, that can save operating cost and reduce noise to spray suction apparatus with oxidation wind in the tower to the pressure of oxidation air.
Technical solution of the present utility model is: it comprises the slurries accelerating tube, slurries dilatation aspiration channel, the aspiration channel sleeve pipe, oxidation air-slurries mixing tube and oxidation air suction line, the slurries accelerating tube is the conical pipe that internal diameter diminishes gradually from liquid feeding end to outlet end, slurries dilatation aspiration channel is that tube wall is provided with a plurality of air admission holes, internal diameter becomes large conical pipe gradually from liquid feeding end to outlet end, the aspiration channel sleeve pipe is that internal diameter is broad in the middle, pipe closes up at two ends small in ends, oxidation air-slurries mixing tube is straight tube, the aspiration channel casing pipe sleeve is outside at slurries dilatation aspiration channel, the outlet end of slurries accelerating tube axially is connected with an end of slurries dilatation aspiration channel liquid feeding end and aspiration channel sleeve pipe, be connected between slurries accelerating tube and the slurries dilatation aspiration channel, the other end of aspiration channel sleeve pipe is connected with the liquid feeding end of oxidation air-slurries mixing tube, have annular oxidation wind between aspiration channel sleeve pipe and the slurries dilatation aspiration channel and suck the gap, have annular air-breathing gap between the inwall of the unsettled position that is connected in oxidation wind sleeve pipe and with aspiration channel sleeve pipe and oxidation air-slurries mixing tube of the outlet end of slurries dilatation aspiration channel, an end of oxidation airduct laterally is connected with oxidation wind sleeve pipe, the other end extends to that desulfuration absorbing tower is outer to be connected to slurries with low-pressure oxidized blower fan or atmosphere oxidation air is provided.
Technique effect of the present utility model is: it can suck fast oxidation air and oxidation air is fully mixed with treating the oxidation slurries, pressure to oxidation wind requires lower, dependence to oxidation fan is lower, can reduce investment outlay and operating cost, reduces to move noise.The slurries that this device is collected with desulfuration absorbing tower high potential energy slurries gathering-device when desulfuration absorbing tower uses are as power, in course of injection, fully mix with the oxidation air suction and with treating the oxidation slurries, finish major part and treat the oxidation of oxidation slurries, all the other oxidation airs flow back to the middle and lower part, absorption tower in company with slurry stream, bring oxidation wind into the absorption tower middle and lower part, continue to finish the oxidation of slurries.
This device has following function:
1, this device can make the high potential energy slurries in the decline process oxidation air be sucked and fully mix with treating the oxidation slurries, finishes most of oxidizing process;
2, the oxidation air that the injection slurry stream that is lowered by sucks is injected into behind the slurry pool of absorption tower middle and lower part at the inner rising of slurry pool, further finishes oxidation;
4, the slurry stream that descends is sprayed and is sucked oxidation air, realizes replacing oxidation fan or reduces the effect that oxidation fan is exerted oneself, and realizes the absorption tower energy-saving run;
5, can realize that oxidation wind " the autonomous suction " or cooperation low-head oxidation fan use, the method of operation of oxidation wind " the autonomous suction " does not need oxidation fan, the pressure head of low-head oxidation fan is the 3-15% of conventional oxidation blower fan (roots blower or centrifugal high pressure fan etc.) pressure head, flow is lower than the 10-25% of conventional oxidation blower fan, and the method for operation is flexible;
6, desulphurization system has been cancelled traditional oxidation fan (roots blower or centrifugal high pressure fan), greatly reduces the operation noise.
Description of drawings
Fig. 1 is the utility model example structure schematic diagram.
The specific embodiment
Desulfuration absorbing tower sprays suction apparatus with oxidation wind in the tower, as shown in Figure 1, it comprises slurries accelerating tube 1, slurries dilatation aspiration channel 2, aspiration channel sleeve pipe 3, oxidation air-slurries mixing tube 4 and oxidation air suction line 5, the conical pipe that slurries accelerating tube 1 diminishes from liquid feeding end to outlet end gradually for internal diameter, slurries dilatation aspiration channel 2 is provided with a plurality of air admission holes 21 for tube wall, internal diameter becomes large conical pipe gradually from liquid feeding end to outlet end, aspiration channel sleeve pipe 3 is that internal diameter is broad in the middle, pipe closes up at two ends small in ends, oxidation air-slurries mixing tube 4 is straight tube, aspiration channel sleeve pipe 3 is enclosed within slurries dilatation aspiration channel 2 outsides, the outlet end of slurries accelerating tube 1 axially is connected with an end of slurries dilatation aspiration channel 2 liquid feeding ends and aspiration channel sleeve pipe 3, be connected between slurries accelerating tube 1 and the slurries dilatation aspiration channel 2, the other end of aspiration channel sleeve pipe 3 is connected with the liquid feeding end of oxidation air-slurries mixing tube 4, has annular oxidation wind gap 31 between aspiration channel sleeve pipe 3 and the slurries dilatation aspiration channel 2, have annular air-breathing gap 32 between the inwall of the unsettled position that is connected in oxidation wind sleeve pipe 3 and with aspiration channel sleeve pipe 3 and oxidation air-slurries mixing tube 4 of the outlet end of slurries dilatation aspiration channel 2, an end of oxidation air suction line 5 laterally is connected with oxidation wind sleeve pipe 3, the other end extends to that desulfuration absorbing tower is outer to be connected to slurries with low-pressure oxidized blower fan or atmosphere oxidation air is provided.
Slurries accelerating tube 1 outlet end internal diameter is identical with slurries dilatation aspiration channel 2 liquid feeding end internal diameters.Aspiration channel sleeve pipe 3 is connected with slurries dilatation aspiration channel 2 with slurries accelerating tube 1 and holds internal diameter identical with slurries dilatation aspiration channel 2 liquid feeding end external diameters with slurries accelerating tube 1 outlet end external diameter.Aspiration channel sleeve pipe 3 is connected with oxidation air-slurries mixing tube 4 and holds internal diameter identical with oxidation air-slurries mixing tube 4 liquid feeding end internal diameters.Slurries dilatation aspiration channel 2 outlet end external diameters link to each other with aspiration channel sleeve pipe 3 less than oxidation air-slurries mixing tube 4 and hold internal diameter.
Slurries fall along the slurries conduit after being collected by slurry collecting disc, because the effect of gravitional force has certain falling speed, the lower end of slurries conduit links to each other with the liquid feeding end of slurries accelerating tube 1, and slurries can be improved to the less outlet end Rapid Flow falling speed of lower time of internal diameter fast by the larger liquid feeding end of slurries accelerating tube 1 internal diameter.Flow into behind the slurries dilatation aspiration channel 2 because caliber becomes large gradually, the slurry stream that Rapid Flow is crossed can suck oxidation air from slurries dilatation aspiration channel 2 each suction hole 21 automatically, pressure to oxidation air requires lower, dependence to oxidation fan also can reduce, can use the lower fan with low voltage of blast that oxidation wind is provided or do not use blower fan, reach the purpose that reduces energy consumption and noise.Slurries behind the suction oxidation air flow out and continue to suck oxidation wind from the annular air-breathing gap between aspiration channel sleeve pipe 3 and the oxidation air-slurries mixing tube 4 from slurries dilatation aspiration channel 2 fast and flow into fast oxidation air-slurries mixing tube 4 again, by the slurries behind oxidation air-slurries mixing tube 4 slurries in the stock tank are produced percussion, oxidation wind is fully mixed with slurries, can reduce the operating cost of desulfuration absorbing tower.
Claims (5)
1. desulfuration absorbing tower sprays suction apparatus with oxidation wind in the tower, it is characterized in that: it comprises slurries accelerating tube (1), slurries dilatation aspiration channel (2), aspiration channel sleeve pipe (3), oxidation air-slurries mixing tube (4) and oxidation air suction line (5), the conical pipe that slurries accelerating tube (1) diminishes from liquid feeding end to outlet end gradually for internal diameter, slurries dilatation aspiration channel (2) is provided with a plurality of air admission holes (21) for tube wall, internal diameter becomes large conical pipe gradually from liquid feeding end to outlet end, aspiration channel sleeve pipe (3) is that internal diameter is broad in the middle, pipe closes up at two ends small in ends, oxidation air-slurries mixing tube (4) is straight tube, aspiration channel sleeve pipe (3) is enclosed within slurries dilatation aspiration channel (2) outside, the outlet end of slurries accelerating tube (1) axially is connected with an end of slurries dilatation aspiration channel (2) liquid feeding end and aspiration channel sleeve pipe (3), be connected between slurries accelerating tube (1) and the slurries dilatation aspiration channel (2), the other end of aspiration channel sleeve pipe (3) is connected with the liquid feeding end of oxidation air-slurries mixing tube (4), has annular oxidation wind gap (31) between aspiration channel sleeve pipe (3) and the slurries dilatation aspiration channel (2), the outlet end of slurries dilatation aspiration channel (2) is unsettled be positioned at oxidation wind sleeve pipe (3) and the inwall of the position that is connected with aspiration channel sleeve pipe (3) and oxidation air-slurries mixing tube (4) between have annular air-breathing gap (32), an end of oxidation air suction line (5) laterally is connected with oxidation wind sleeve pipe (3), the other end extends to that desulfuration absorbing tower is outer to be connected to slurries with low-pressure oxidized blower fan or atmosphere oxidation air is provided.
2. desulfuration absorbing tower as claimed in claim 1 sprays suction apparatus with oxidation wind in the tower, it is characterized in that described slurries accelerating tube (1) outlet end internal diameter is identical with slurries dilatation aspiration channel (2) liquid feeding end internal diameter.
3. desulfuration absorbing tower as claimed in claim 1 sprays suction apparatus with oxidation wind in the tower, it is characterized in that described aspiration channel sleeve pipe (3) and slurries accelerating tube (1) are connected with slurries dilatation aspiration channel (2) to hold internal diameter identical with slurries dilatation aspiration channel (2) liquid feeding end external diameter with slurries accelerating tube (1) outlet end external diameter.
4. desulfuration absorbing tower as claimed in claim 1 sprays suction apparatus with oxidation wind in the tower, it is characterized in that described aspiration channel sleeve pipe (3) is connected with oxidation air-slurries mixing tube (4) to hold internal diameter identical with oxidation air-slurries mixing tube (4) liquid feeding end internal diameter.
5. desulfuration absorbing tower as claimed in claim 1 sprays suction apparatus with oxidation wind in the tower, it is characterized in that described slurries dilatation aspiration channel (2) outlet end external diameter links to each other with aspiration channel sleeve pipe (3) less than oxidation air-slurries mixing tube (4) to hold internal diameter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220361928 CN202700360U (en) | 2012-07-25 | 2012-07-25 | Oxidation air spraying and sucking device used in desulfurizing absorption tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220361928 CN202700360U (en) | 2012-07-25 | 2012-07-25 | Oxidation air spraying and sucking device used in desulfurizing absorption tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202700360U true CN202700360U (en) | 2013-01-30 |
Family
ID=47580701
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220361928 Expired - Lifetime CN202700360U (en) | 2012-07-25 | 2012-07-25 | Oxidation air spraying and sucking device used in desulfurizing absorption tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202700360U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102728211A (en) * | 2012-07-25 | 2012-10-17 | 王秋平 | Device for injecting and inhaling in-tower oxidized air for desulfurizing absorption tower |
| CN106975375A (en) * | 2017-05-02 | 2017-07-25 | 江苏揽山环境科技股份有限公司 | Micro bubble apparatus, desulphurization plant, oxidation and the method for lifting oxygen content of water |
-
2012
- 2012-07-25 CN CN 201220361928 patent/CN202700360U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102728211A (en) * | 2012-07-25 | 2012-10-17 | 王秋平 | Device for injecting and inhaling in-tower oxidized air for desulfurizing absorption tower |
| CN102728211B (en) * | 2012-07-25 | 2014-01-15 | 王秋平 | Device for injecting and inhaling in-tower oxidized air for desulfurizing absorption tower |
| CN106975375A (en) * | 2017-05-02 | 2017-07-25 | 江苏揽山环境科技股份有限公司 | Micro bubble apparatus, desulphurization plant, oxidation and the method for lifting oxygen content of water |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20130130 Effective date of abandoning: 20140115 |
|
| RGAV | Abandon patent right to avoid regrant |