CN204380493U - A kind of dusty gas cleaning system for power industry high reactivity - Google Patents
A kind of dusty gas cleaning system for power industry high reactivity Download PDFInfo
- Publication number
- CN204380493U CN204380493U CN201420775537.0U CN201420775537U CN204380493U CN 204380493 U CN204380493 U CN 204380493U CN 201420775537 U CN201420775537 U CN 201420775537U CN 204380493 U CN204380493 U CN 204380493U
- Authority
- CN
- China
- Prior art keywords
- gas
- liquid
- pipeline
- ozone
- reactions
- 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
Links
Abstract
The utility model relates to a kind of dusty gas cleaning system for power industry high reactivity.The utility model is by gas solid/liquid/gas reactions pipeline, the ozone supplied pipeline be connected with gas solid/liquid/gas reactions pipeline front end, the gas liquid reaction tower be connected with gas solid/liquid/gas reactions line end, the spray equipment being arranged at gas liquid reaction tower top end top and the reactant liquor reclaim line being arranged at gas liquid reaction tower bottom composition, Time and place during ozone purification is reacted by the utility model is optimized, solve the inhomogeneities in space, thus make ozone in the reaction utilization rate close to 100%, and reacted gas is reclaimed by gas liquid reaction, continue secondary to utilize, both improve reaction efficiency, also add the income of accessory substance simultaneously.
Description
Technical field
The utility model relates to a kind of dusty gas cleaning system for power industry high reactivity.
Background technology
In power industry is produced, often environmental issue is come from for maximum problem enterprise, the process of tail gas is a then primary difficult problem wherein especially, ozone improvement sewage is utilized to become the treatment technology of an extensive use, the plurality of advantages such as pollution is little although ozone has, no pollution, but the cost in recent years due to ozone is high, if react insufficient, then cause the problem of high cost, it is caused to be difficult to promote, current technology reactivity is still difficult to promote, and makes ozone be difficult to promote as the mode of exhaust emissions.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of dusty gas cleaning system for power industry high reactivity.
The utility model adopts following technical scheme:
The utility model is made up of gas solid/liquid/gas reactions pipeline, the ozone supplied pipeline be connected with gas solid/liquid/gas reactions pipeline front end, the gas liquid reaction tower be connected with gas solid/liquid/gas reactions line end, the spray equipment being arranged at gas liquid reaction tower top end top and the reactant liquor reclaim line that is arranged at gas liquid reaction tower bottom
Described ozone supplied pipeline is made up of ozone main pipeline, more than one ozone sub-pipes and more than one circular aerated conduit, described ozone main pipeline is connected with circular aerated conduit by ozone sub-pipes, described circular aerated conduit is provided with more than one venthole
Described gas liquid reaction tower is arranged at the spiral wing plate of hollow type in cylindrical tower body by cylindrical tower body and circumference, described cylindrical tower body bottom is provided with the air inlet be connected with gas solid/liquid/gas reactions line end and the liquid outlet be connected with reactant liquor reclaim line forms, the upper edge of described liquid outlet is lower than the lower edge of described air inlet, the gas spoiler that the helically formula lift structure that the spiral wing plate of described hollow type is arranged at cylindrical tower body inwall by two or more is arranged forms, interval is provided with between described gas spoiler
Described spray equipment comprises water inlet pipe, the more than one shower be connected with water inlet pipe and the more than one spray head be arranged on shower,
Described reactant liquor reclaim line comprises the devil liquor recovery pipeline be connected with liquid outlet.
Good effect of the present utility model is as follows:
Time and place during ozone purification is reacted by the utility model is optimized, in gas solid/liquid/gas reactions (ozone and tail gas), the ozone gas of input be that swirling is cut by the venthole of setting oblique on circular aerated conduit by ozone, thus solve the inhomogeneities of time, again the mist through gas solid/liquid/gas reactions is entered along tower wall tangential direction, broken up by spoiler, the air-flow of spoiler upper end forms cyclone and moves upward along tower wall, the air-flow of lower end forms negative pressure and upwards collects from tower body center, solve the inhomogeneities in space, thus make ozone in the reaction utilization rate close to 100%, and reacted gas is reclaimed by gas liquid reaction, continue secondary to utilize, both improve reaction efficiency, also add the income of accessory substance simultaneously.
Accompanying drawing explanation
Accompanying drawing 1 is the utility model structural representation.
Accompanying drawing 2 is the utility model ozone supplied pipeline induction part structural representation.
Accompanying drawing 3 is the utility model ozone supplied pipeline outlet gas part structural representation.
Accompanying drawing 4 is the utility model reactant liquor reclaim line sectional structure schematic diagram.
Accompanying drawing 5 overlooks apparatus structure schematic diagram for the utility model reactant liquor reclaim line.
Detailed description of the invention
As shown in accompanying drawing 1-5, the utility model is made up of gas solid/liquid/gas reactions pipeline 1, the ozone supplied pipeline 2 be connected with gas solid/liquid/gas reactions pipeline 1 front end, the gas liquid reaction tower 3 be connected with gas solid/liquid/gas reactions pipeline 1 end, the spray equipment 4 being arranged at gas liquid reaction tower top end 3 top and the reactant liquor reclaim line 5 be arranged at bottom gas liquid reaction tower 3
Described ozone supplied pipeline 2 is made up of ozone main pipeline 2-1, more than one ozone sub-pipes 2-2 and more than one circular aerated conduit 2-3, described ozone main pipeline 2-1 is connected with circular aerated conduit 2-3 by ozone sub-pipes 2-2, described circular aerated conduit 2-3 is provided with more than one venthole 2-4
Described gas liquid reaction tower 3 is arranged at the spiral wing plate of hollow type in cylindrical tower body 3-1 by cylindrical tower body 3-1 and circumference, described cylindrical tower body 3-1 bottom is provided with the air inlet 3-2 be connected with gas solid/liquid/gas reactions pipeline 1 end and forms the liquid outlet 3-4 be connected with reactant liquor reclaim line 5, the upper edge of described liquid outlet 3-4 is lower than the lower edge of described air inlet 3-2, the gas spoiler 3-3 that the helically formula lift structure that the spiral wing plate of described hollow type is arranged at cylindrical tower body 3-1 inwall by two or more is arranged forms, interval is provided with between described gas spoiler 3-3,
Described spray equipment 4 comprises water inlet pipe 4-1, the more than one shower 4-2 be connected with water inlet pipe 4-1 and the more than one spray head 4-3 be arranged on shower 4-2,
Described reactant liquor reclaim line 5 comprises the devil liquor recovery pipeline 5-1 be connected with liquid outlet 3-4,
The opening direction of described air inlet 3-2 is the tangential direction of described cylindrical tower body 3-1, and described gas solid/liquid/gas reactions pipeline 1 is arranged along the tangent line bearing of trend of cylindrical tower body 3-1.
Time and place during ozone purification is reacted by the utility model is optimized, in gas solid/liquid/gas reactions (ozone and tail gas), the ozone gas of input be that swirling is cut by the venthole of setting oblique on circular aerated conduit by ozone, thus solve the inhomogeneities of time, again the mist through gas solid/liquid/gas reactions is entered along tower wall tangential direction, broken up by spoiler, the air-flow of spoiler upper end forms cyclone and moves upward along tower wall, the air-flow of lower end forms negative pressure and upwards collects from tower body center, solve the inhomogeneities in space, thus make ozone in the reaction utilization rate close to 100%, and reacted gas is reclaimed by gas liquid reaction, continue secondary to utilize, both improve reaction efficiency, also add the income of accessory substance simultaneously.
Claims (1)
1. the dusty gas cleaning system for power industry high reactivity, it is characterized in that it is made up of gas solid/liquid/gas reactions pipeline (1), the ozone supplied pipeline (2) be connected with gas solid/liquid/gas reactions pipeline (1) front end, the gas liquid reaction tower (3) be connected with gas solid/liquid/gas reactions pipeline (1) end, the spray equipment (4) being arranged at gas liquid reaction tower (3) top, top and the reactant liquor reclaim line (5) be arranged at bottom gas liquid reaction tower (3)
Described ozone supplied pipeline (2) is made up of ozone main pipeline (2-1), more than one ozone sub-pipes (2-2) and more than one circular aerated conduit (2-3), described ozone main pipeline (2-1) is connected with circular aerated conduit (2-3) by ozone sub-pipes (2-2), described circular aerated conduit (2-3) is provided with more than one venthole (2-4)
Described gas liquid reaction tower (3) is arranged at the spiral wing plate of hollow type in cylindrical tower body (3-1) by cylindrical tower body (3-1) and circumference, described cylindrical tower body (3-1) bottom is provided with the air inlet (3-2) be connected with gas solid/liquid/gas reactions pipeline (1) end and the liquid outlet (3-4) be connected with reactant liquor reclaim line (5) forms, the upper edge of described liquid outlet (3-4) is lower than the lower edge of described air inlet (3-2), the gas spoiler (3-3) that the helically formula lift structure that the spiral wing plate of described hollow type is arranged at cylindrical tower body (3-1) inwall by two or more is arranged forms, interval is provided with between described gas spoiler (3-3),
Described spray equipment (4) comprises water inlet pipe (4-1), the more than one shower (4-2) be connected with water inlet pipe (4-1) and the more than one spray head (4-3) be arranged on shower (4-2),
Described reactant liquor reclaim line (5) comprises the devil liquor recovery pipeline (5-1) be connected with liquid outlet (3-4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420775537.0U CN204380493U (en) | 2014-12-11 | 2014-12-11 | A kind of dusty gas cleaning system for power industry high reactivity |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420775537.0U CN204380493U (en) | 2014-12-11 | 2014-12-11 | A kind of dusty gas cleaning system for power industry high reactivity |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204380493U true CN204380493U (en) | 2015-06-10 |
Family
ID=53353250
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420775537.0U Expired - Fee Related CN204380493U (en) | 2014-12-11 | 2014-12-11 | A kind of dusty gas cleaning system for power industry high reactivity |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204380493U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114053856A (en) * | 2020-07-31 | 2022-02-18 | 河南智川节能环保科技有限公司 | A gaseous pollutants clean system for electric power industry high reaction rate |
-
2014
- 2014-12-11 CN CN201420775537.0U patent/CN204380493U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114053856A (en) * | 2020-07-31 | 2022-02-18 | 河南智川节能环保科技有限公司 | A gaseous pollutants clean system for electric power industry high reaction rate |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107162158B (en) | Fenton fluidized bed reactor and method | |
| CN204474409U (en) | Rectilinear anaerobic aerobic integratedization reactor | |
| CN203678369U (en) | Circulating cooling system of reaction kettle | |
| CN105080291A (en) | Device for improving industrial tail gas cleaning effects | |
| CN204380493U (en) | A kind of dusty gas cleaning system for power industry high reactivity | |
| CN204380496U (en) | A kind of low-loss high efficiency power industry dusty gas cleaning system | |
| CN204447705U (en) | A kind of power industry exhaust gas purification system with the spiral wing plate of hollow type | |
| CN204638201U (en) | A kind of desulfurizing agent vacuum condensation liquid processing device | |
| CN204147736U (en) | The spray recovery system of tail gas | |
| CN204485638U (en) | Mixing two-phase desulfuring and denitrifying dedust apparatus | |
| CN203954983U (en) | Composite type desulfurating dust removing device for flue gas | |
| CN203938621U (en) | A kind of by the refining isobutyric suite of equipment of isobutyric aldehyde | |
| CN205569873U (en) | Multistage siphon separator that hydrolysises of living beings | |
| CN204170606U (en) | Acid hydrolysis tail gas venturi spray absorber | |
| CN204958683U (en) | Synthetic effluent disposal system of resin | |
| CN204550195U (en) | EGSB anaerobic sludge refluxing reactor | |
| CN205570006U (en) | Digester environmental protection dust collector | |
| CN209612568U (en) | A kind of void tower device of PLC control high-temperature flue gas | |
| CN204417158U (en) | A kind of novel sewage treatment unit | |
| CN213771485U (en) | Anaerobic reactor | |
| CN204034518U (en) | Produce the emission-control equipment of styrene-butadiene latex water reducer | |
| CN102836633A (en) | Absorption tower | |
| CN202173879U (en) | Absorption tower | |
| CN205443027U (en) | Mud sewage purification processing device | |
| CN205367871U (en) | Tertiary anaerobic fermentation device |
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: 20150610 Termination date: 20151211 |
|
| EXPY | Termination of patent right or utility model |