CN204619733U - Half dry type reaction tower - Google Patents
Half dry type reaction tower Download PDFInfo
- Publication number
- CN204619733U CN204619733U CN201520105347.2U CN201520105347U CN204619733U CN 204619733 U CN204619733 U CN 204619733U CN 201520105347 U CN201520105347 U CN 201520105347U CN 204619733 U CN204619733 U CN 204619733U
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- CN
- China
- Prior art keywords
- flue
- spiral case
- air intake
- dust retainer
- reaction tower
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- Expired - Fee Related
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Abstract
The utility model relates to fume treatment technical field, especially half dry type reaction tower, comprise tower body, air intake spiral case, sprayer, motor, smoke distributor, neat stress exports, cinder-discharging port and flue-dust retainer, tower body top arranges air intake spiral case, air intake spiral case air outlet is communicated with smoke distributor, vertically motor is fixed with in the middle part of smoke distributor, motor is driven by shaft coupling and connects sprayer, tower body bottom is fixedly connected with flue-dust retainer, flue-dust retainer upper portion side wall is provided with neat stress outlet, cinder-discharging port is provided with bottom flue-dust retainer, described air intake spiral case air inlet is communicated with bellows, air inlet and the air outlet place of described bellows are respectively equipped with sieve plate.The half dry type reaction tower that the utility model provides, effectively can prevent the air inlet junction disrepair phenomenon of air inlet pipe and air intake spiral case, by arranging sieve plate, effectively can stop that the larger light materials in flue gas is sent in reaction tower with flue gas, preventing smoke distributor to block.
Description
Technical field
The utility model relates to fume treatment technical field, especially half dry type reaction tower.
Background technology
Along with the development of society, the quickening of process of industrialization, and the pollution of environment is more and more serious, the waste gas produced in industrial gasses and process refuse rubbish process pollutes air, need the air cleaning facility of more and more function admirable, the purification techniques of waste gas mainly contains wet method, dry method and semidry method three kinds, wet cleaning efficiency is high, but there is sewage handling problem, although dry method does not have sewage handling problem, but purification efficiency is low, semidry method combines the advantage of wet method and dry method, do not have sewage discharge and also purification efficiency high.
Half dry type reaction tower is as important semidry method trash-removal device, in actual use, because the flue-gas temperature entered is very high, due to reason of expanding with heat and contract with cold, the air inlet junction of air inlet pipe and air intake spiral case is easy to occur the phenomenons such as crack breakage, and send in reaction tower containing larger light materials with flue gas in flue gas, usually cause smoke distributor to block, cause purification efficiency in reaction tower to reduce.
Utility model content
The technical problems to be solved in the utility model is: easily break in order to the air inlet junction solving air inlet pipe and air intake spiral case and prevent larger light materials from entering the problem of reaction tower with flue gas, the utility model provides half dry type reaction tower, by arranging bellows, and at the air inlet of bellows and air outlet, sieve plate being set respectively, easily break and prevent larger light materials from entering the problem of reaction tower with flue gas in the air inlet junction effectively solving air inlet pipe and air intake spiral case.
The utility model solves the technical scheme that its technical problem adopts: a kind of half dry type reaction tower, comprise tower body, air intake spiral case, sprayer, motor, smoke distributor, neat stress exports, cinder-discharging port and flue-dust retainer, tower body top arranges air intake spiral case, air intake spiral case air outlet is communicated with smoke distributor, vertically motor is fixed with in the middle part of smoke distributor, motor is driven by shaft coupling and connects sprayer, tower body bottom is fixedly connected with flue-dust retainer, flue-dust retainer upper portion side wall is provided with neat stress outlet, cinder-discharging port is provided with bottom flue-dust retainer, described air intake spiral case air inlet is communicated with bellows, air inlet and the air outlet place of described bellows are respectively equipped with sieve plate.
Further, the sidewall of described smoke distributor is provided with the opening that several change flue gas direction, is changed the direction of flue gas by opening, makes the abundant haptoreaction of medicament that flue gas can spray with sprayer.
Further, described flue-dust retainer lower sides is provided with manhole, facilitates people to enter maintenance flue-dust retainer.
Particularly, described cinder-discharging port is fixedly connected with electric cinder valve.
The beneficial effects of the utility model are: the half dry type reaction tower that the utility model provides, effectively can prevent the air inlet junction disrepair phenomenon of air inlet pipe and air intake spiral case, by arranging sieve plate, effectively can stop that the larger light materials in flue gas is sent in reaction tower with flue gas, smoke distributor is prevented to block, avoid the reduction of purification efficiency in reaction tower, save the cost of overhaul.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Fig. 1 is the structural representation of half dry type reaction tower of the present utility model;
Fig. 2 is the enlarged drawing of A in Fig. 1.
Wherein: 1. tower body; 2. air intake spiral case; 3. sprayer; 4. motor; 5. smoke distributor; 6. neat stress outlet; 7. cinder-discharging port; 8. bellows; 9, sieve plate; 10. opening; 11. manholes; 12. flue-dust retainers; 13. electric cinder valves.
Detailed description of the invention
By reference to the accompanying drawings the utility model is described in further detail now.These accompanying drawings are the schematic diagram of simplification, only basic structure of the present utility model are described in a schematic way, and therefore it only shows the formation relevant with the utility model.
As depicted in figs. 1 and 2, a kind of half dry type reaction tower, comprise tower body 1, air intake spiral case 2, sprayer 3, motor 4, smoke distributor 5, neat stress outlet 6, cinder-discharging port 7 and flue-dust retainer 12, tower body 1 top arranges air intake spiral case 2, air intake spiral case 2 air outlet is communicated with smoke distributor 5, motor 4 is vertically fixed with in the middle part of smoke distributor 5, the sidewall of smoke distributor 5 is provided with the opening 10 that several change flue gas direction, motor 4 is driven by shaft coupling and connects sprayer 3, tower body 1 bottom is fixedly connected with flue-dust retainer 12, flue-dust retainer 12 upper portion side wall is provided with neat stress outlet 6, cinder-discharging port 7 is provided with bottom flue-dust retainer 12, cinder-discharging port 7 is fixedly connected with electric cinder valve 13, flue-dust retainer 12 lower sides is provided with manhole 11, air intake spiral case 2 air inlet is communicated with bellows 8, air inlet and the air outlet place of bellows 8 are respectively equipped with sieve plate 9.
During normal work, after flue gas filters larger light materials by sieve plate 9, enter smoke distributor 5, the direction of flue gas is changed by the opening 10 that smoke distributor 5 is arranged, make reaction tower purification efficiency higher, bellows 8 is set and can effectively prevents air intake spiral case 2 air inlet and blast pipe junction from gas leak phenomenon occurring.
With above-mentioned according to desirable embodiment of the present utility model for enlightenment, by above-mentioned description, relevant staff in the scope not departing from this utility model technological thought, can carry out various change and amendment completely.The technical scope of this utility model is not limited to the content on description, must determine its technical scope according to right.
Claims (4)
1. a half dry type reaction tower, comprise tower body (1), air intake spiral case (2), sprayer (3), motor (4), smoke distributor (5), neat stress outlet (6), cinder-discharging port (7) and flue-dust retainer (12), tower body (1) top arranges air intake spiral case (2), air intake spiral case (2) air outlet is communicated with smoke distributor (5), smoke distributor (5) middle part is vertically fixed with motor (4), motor (4) is driven by shaft coupling and connects sprayer (3), tower body (1) bottom is fixedly connected with flue-dust retainer (12), flue-dust retainer (12) upper portion side wall is provided with neat stress outlet (6), flue-dust retainer (12) bottom is provided with cinder-discharging port (7), it is characterized in that: described air intake spiral case (2) air inlet is communicated with bellows (8), the air inlet of described bellows (8) and air outlet place are respectively equipped with sieve plate (9).
2. half dry type reaction tower as claimed in claim 1, is characterized in that: the sidewall of described smoke distributor (5) is provided with the opening (10) that several change flue gas direction.
3. half dry type reaction tower as claimed in claim 1 or 2, is characterized in that: described flue-dust retainer (12) lower sides is provided with manhole (11).
4. half dry type reaction tower as claimed in claim 3, is characterized in that: described cinder-discharging port (7) is fixedly connected with electric cinder valve (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520105347.2U CN204619733U (en) | 2015-02-13 | 2015-02-13 | Half dry type reaction tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520105347.2U CN204619733U (en) | 2015-02-13 | 2015-02-13 | Half dry type reaction tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204619733U true CN204619733U (en) | 2015-09-09 |
Family
ID=54038797
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520105347.2U Expired - Fee Related CN204619733U (en) | 2015-02-13 | 2015-02-13 | Half dry type reaction tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204619733U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108178217A (en) * | 2018-01-08 | 2018-06-19 | 华电水务工程有限公司 | A kind of high slat-containing wastewater is evaporated system and technique |
-
2015
- 2015-02-13 CN CN201520105347.2U patent/CN204619733U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108178217A (en) * | 2018-01-08 | 2018-06-19 | 华电水务工程有限公司 | A kind of high slat-containing wastewater is evaporated system and technique |
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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: 20150909 Termination date: 20210213 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |