CN205127695U - Dry reaction tower - Google Patents
Dry reaction tower Download PDFInfo
- Publication number
- CN205127695U CN205127695U CN201520879073.2U CN201520879073U CN205127695U CN 205127695 U CN205127695 U CN 205127695U CN 201520879073 U CN201520879073 U CN 201520879073U CN 205127695 U CN205127695 U CN 205127695U
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- CN
- China
- Prior art keywords
- reaction tower
- tower
- air inlet
- lower reaction
- nozzle
- 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 - Fee Related
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Abstract
The utility model relates to a dry reaction tower, it includes reaction tower and lower reaction tower, they are connected through the venturi be equipped with the ash hole down bottom the reaction tower upward be equipped with the gas outlet to the side of the reaction tower the reaction tower side is equipped with the air inlet down, the air inlet links to each other with flue gas pipeline the last nozzle I that is equipped with of flue gas pipeline reaction tower upper portion is equipped with nozzle II down. The utility model discloses flue gas reaction, corrosion resisting property is good, reduces the sack load, improves life.
Description
Technical field
The utility model relates to a kind of drying device, is specifically related to a kind of dry reaction tower.
Background technology
At present, half-dried tower runs early stage or the time of parking at incinerator system, flue gas can occur and carry free water problem, thus have a strong impact on the service life of equipment, reduces the operating efficiency of whole system.In existing dry reaction tower, anticorrosion effect is poor, and tower is arranged without nozzle, and flue gas reacts insufficient in tower, and ashes enter cloth bag, considerably increases cloth bag load.
Summary of the invention
Goal of the invention: the purpose of this utility model is to overcome deficiency of the prior art, provides a kind of smoke reaction abundant, corrosion resistance and good, reduces cloth bag load, improve the dry reaction tower in service life.
Technical scheme: in order to solve the problems of the technologies described above, dry reaction tower described in the utility model, it comprises reaction tower and lower reaction tower, they are connected by venturi, bottom described lower reaction tower, be provided with ash hole, and reaction tower side is provided with gas outlet on described, air inlet is provided with in described lower reaction tower side, described air inlet is connected with flue, and described flue is provided with nozzle I, is provided with nozzle II on described lower reaction tower top.
Described upper reaction tower and lower reaction tower are all vertical tower.
Reaction tower and lower reaction tower inwall are all provided with acid and alkali-resistance layer on described.
Described air inlet is located in the middle part of lower reaction tower side.
Star-shaped dust-discharging valve is provided with below described ash hole.
Beneficial effect: the utility model compared with prior art, its remarkable advantage is: the utility model adopts venturi to connect, lower reaction tower, vibrational power flow is reasonable, solve half-dried tower flue gas when incinerator system runs early stage or parking and take free water problem, effective raising whole service life and production efficiency, nozzle I is adopted to spray 200 order active carbons, nozzle II jet paraffin oxidation calcium, flue gas is fully reacted, a large amount of ashes are from the sedimentation of tower body ash hole, greatly reduce the ashes sedimentation in cloth bag, thus greatly reduce the live load of cloth bag, adopt acid and alkali-resistance layer, play good anticorrosion effect, thus improve the service life of equipment.
Accompanying drawing explanation
Fig. 1 is overall structure schematic diagram of the present utility model.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is further described.
As shown in Figure 1, dry reaction tower described in the utility model, it comprises reaction tower 1 and lower reaction tower 2, they are connected by venturi 3, bottom described lower reaction tower 2, be provided with ash hole 4, and reaction tower 1 side is provided with gas outlet 5 on described, air inlet 6 is provided with in described lower reaction tower 2 side, described air inlet 6 is connected with flue 7, and described flue 7 is provided with nozzle I 8, is provided with nozzle II 9 on described lower reaction tower 2 top; Described upper reaction tower 1 and lower reaction tower 2 are all vertical tower; Reaction tower 1 and lower reaction tower 2 inwall are all provided with acid and alkali-resistance layer 10 on described; Described air inlet 6 is located in the middle part of lower reaction tower 2 side; Star-shaped dust-discharging valve 11 is provided with below described ash hole 4.The utility model adopts venturi to connect, lower reaction tower, vibrational power flow is reasonable, solve half-dried tower flue gas when incinerator system runs early stage or parking and take free water problem, effective raising whole service life and production efficiency, nozzle I is adopted to spray 200 order active carbons, nozzle II jet paraffin oxidation calcium, flue gas is fully reacted, a large amount of ashes are from the sedimentation of tower body ash hole, greatly reduce the ashes sedimentation in cloth bag, thus greatly reduce the live load of cloth bag, adopt acid and alkali-resistance layer, play good anticorrosion effect, thus improve the service life of equipment.
The utility model provides a kind of thinking and method; the method and access of this technical scheme of specific implementation is a lot; the above is only preferred embodiment of the present utility model; should be understood that; for those skilled in the art, under the prerequisite not departing from the utility model principle, some improvements and modifications can also be made; these improvements and modifications also should be considered as protection domain of the present utility model, and all available prior art of each part not clear and definite in the present embodiment is realized.
Claims (5)
1. dry reaction tower, it is characterized in that: it comprises reaction tower (1) and lower reaction tower (2), they are connected by venturi (3), ash hole (4) is provided with in described lower reaction tower (2) bottom, reaction tower (1) side is provided with gas outlet (5) on described, air inlet (6) is provided with in described lower reaction tower (2) side, described air inlet (6) is connected with flue (7), described flue (7) is provided with nozzle I (8), is provided with nozzle II (9) on described lower reaction tower (2) top.
2. dry reaction tower according to claim 1, is characterized in that: described upper reaction tower (1) and lower reaction tower (2) are all vertical tower.
3. dry reaction tower according to claim 1, is characterized in that: reaction tower (1) and lower reaction tower (2) inwall are all provided with acid and alkali-resistance layer (10) on described.
4. dry reaction tower according to claim 1, is characterized in that: described air inlet (6) is located in the middle part of lower reaction tower (2) side.
5. dry reaction tower according to claim 1, is characterized in that: be provided with star-shaped dust-discharging valve (11) in described ash hole (4) below.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520879073.2U CN205127695U (en) | 2015-11-06 | 2015-11-06 | Dry reaction tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520879073.2U CN205127695U (en) | 2015-11-06 | 2015-11-06 | Dry reaction tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205127695U true CN205127695U (en) | 2016-04-06 |
Family
ID=55613520
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520879073.2U Expired - Fee Related CN205127695U (en) | 2015-11-06 | 2015-11-06 | Dry reaction tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205127695U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106669378A (en) * | 2015-11-06 | 2017-05-17 | 江苏大信环境科技有限公司 | Drying reaction tower |
-
2015
- 2015-11-06 CN CN201520879073.2U patent/CN205127695U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106669378A (en) * | 2015-11-06 | 2017-05-17 | 江苏大信环境科技有限公司 | Drying reaction tower |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160406 Termination date: 20171106 |