CN201799202U - Combined waste gas treatment device of tornado tower - Google Patents
Combined waste gas treatment device of tornado tower Download PDFInfo
- Publication number
- CN201799202U CN201799202U CN201020501340XU CN201020501340U CN201799202U CN 201799202 U CN201799202 U CN 201799202U CN 201020501340X U CN201020501340X U CN 201020501340XU CN 201020501340 U CN201020501340 U CN 201020501340U CN 201799202 U CN201799202 U CN 201799202U
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- airduct
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- water tank
- tank device
- cyclone separator
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Abstract
The utility model discloses a combined waste gas treatment device of a tornado tower, which relates to a waste gas treatment device and consists of a fan base (1), a centrifugal fan (2), a first air tube (3), a drain pipe (4), a venturi tube (5), a cyclone separator (6), a circulating water tank device (7) and a second air tube (8), wherein the fan base (1) is provided with the centrifugal fan (2), the centrifugal fan (2) is connected with the first air tube (3), the first air tube (3) is connected with the venturi tube (5), the venturi tube (5) is connected with the second air tube (8), the second air tube (8) is connected with the cyclone separator (6), the circulating water tank device (7) is connected with the bottom of the cyclone separator (6), the first air tube (3) is connected with the circulating water tank device (7) via the drain pipe (4), and a water spray device in the venturi tube (5) is connected with the circulating water tank device (7) via a pipe and a valve. The device can improve the waste gas treatment performance, and effectively reduces operation and maintenance costs.
Description
Technical field:
The utility model relates to a kind of emission-control equipment, relates in particular to a kind of whirlwind tower combined exhaust gas treating apparatus.
Background technology:
For a long time, PCB and electroplating industry production line treatment of waste gas device adopt traditional mode always, and be unalterable, promptly with the method for packed absorber or spray absorber, active carbon (or other material filtering layer) filter (cloth) layer.Wherein there is the situation of filler or the easy contaminated obstruction of filter (cloth) layer in stuffing process and active carbon (or other material filtering layer) filter (cloth) layer method, cause problems such as the device processes quantitative change is little, process result degrades, therefore cause problems such as treatment effect instability, filtrate frequent clean or the frequent replacing of filter (cloth) layer, cause a series of problems such as operation and maintenance cost is higher.This has increased the risk of environmental pollution and the production cost of manufacturer undoubtedly greatly.
The utility model content:
The purpose of this utility model provides a kind of whirlwind tower combined exhaust gas treating apparatus, and it can improve the treatment of waste gas performance, effectively reduces operation and maintenance cost.
In order to solve the existing problem of background technology, the utility model is by the following technical solutions: it is by base plate, centrifugal blower, first airduct, drainpipe, Venturi tube, cyclone separator, the cyclic water tank device and second airduct are formed, base plate is provided with centrifugal blower, centrifugal blower links to each other with first airduct, first airduct links to each other with Venturi tube, Venturi tube links to each other with second airduct, second airduct links to each other with cyclone separator, the cyclic water tank device links to each other with the bottom of cyclone separator, first airduct links to each other with the cyclic water tank device by drainpipe, and the water injector in the Venturi tube links to each other with the cyclic water tank device with valve by pipe.
Described first airduct comprises first access hole and water fender, and first access hole is arranged on the afterbody top of first airduct, and water fender is arranged on the afterbody below inwall of first airduct.
Described Venturi tube comprises collapsible tube, trunnion and convergent divergent channel, and an end of collapsible tube links to each other with first airduct, and the other end links to each other with trunnion, and trunnion links to each other with convergent divergent channel, and convergent divergent channel links to each other with second airduct.
Described cyclone separator comprises central tube, bypass pipe and detection hole, and the arranged outside of cyclone separator has bypass pipe, and central tube vertically is vertically set on cyclone separator inside center position, and central tube is provided with and detects the hole.
Described cyclic water tank device comprises fixed support, water circulating pump and rainhat, and fixed support is provided with water circulating pump, and water circulating pump is provided with rainhat, and water circulating pump links to each other with cyclic water tank device and Venturi tube with valve by pipe.
Described second airduct is provided with second access hole, and the water injector in second airduct links to each other with the cyclic water tank device with valve by pipe.
Venturi tube described in the utility model-whirlwind tower composite set includes Venturi tube mixed zone and the gas-liquid-solid Disengagement zone of whirlwind tower and transition region therebetween, is made by plastic plate or other metals and anti-corrosion material integral body.The utility model also is provided with cat ladder and guardrail, detection platform and guardrail and lightning arrester in addition.Wherein, waste gas acutely clashes into mixing with absorption liquid in Venturi tube, make that the harmful components in the waste gas are dissolved in the absorption liquid, and the organic matter of dust in the waste gas or chance cold curing is all swept and is involved in the absorption liquid simultaneously.The mixture that contains gas-liquid-solid three-phase material enters in the cyclone separating tower subsequently, cyclone separating tower is provided with the central row tracheae, gas enters from tower upper end tangent line, circle ring area between tower wall and central tube rotates and descends then, at last, heavy drop and solid matter fall into circulating slot, and the tail gas after the purification is discharged by central tube.
The utility model has the advantages that: its can improve exhaust-gas treatment economical, stable, efficiently, reduces significantly than conventional process plant area area and weight of equipment and size; Prevent the obstruction of solid particulate matter in the waste gas (comprising the organic class particle that freezes) effectively, thereby reduce the operation cost of factory significantly packing layer or filtration (cloth) layer; The design optimization of central tube gas flow, more help the rotation of gas-liquid-solid three-phase mixture, thereby improve separative efficiency.
Description of drawings:
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the vertical view of Fig. 1.
The specific embodiment:
With reference to Fig. 1-2, this specific embodiment is by the following technical solutions: it is by base plate 1, centrifugal blower 2, first airduct 3, drainpipe 4, Venturi tube 5, cyclone separator 6, the cyclic water tank device 7 and second airduct 8 are formed, base plate 1 is provided with centrifugal blower 2, centrifugal blower 2 links to each other with first airduct 3, first airduct 3 links to each other with Venturi tube 5, Venturi tube 5 links to each other with second airduct 8, second airduct 8 links to each other with cyclone separator 6, cyclic water tank device 7 links to each other with the bottom of cyclone separator 6, first airduct 3 links to each other with cyclic water tank device 7 by drainpipe 4, and the water injector in the Venturi tube 5 links to each other with cyclic water tank device 7 with valve by pipe.
Described first airduct 3 comprises the first access hole 3-1 and water fender 3-2, and the first access hole 3-1 is arranged on the afterbody top of first airduct 3, and water fender 3-2 is arranged on the afterbody below inwall of first airduct 3.
Described Venturi tube 5 comprises collapsible tube 5-1, trunnion 5-2 and convergent divergent channel 5-3, and the end of collapsible tube 5-1 links to each other with first airduct 3, and the other end links to each other with trunnion 5-2, and trunnion 5-2 links to each other with convergent divergent channel 5-3, and convergent divergent channel 5-3 links to each other with second airduct 8.
Described cyclone separator 6 comprises central tube 6-1, bypass pipe 6-2 and detects hole 6-3, the arranged outside of cyclone separator 6 has bypass pipe 6-2, central tube 6-1 vertically is vertically set on cyclone separator 6 inside center positions, and central tube 6-1 is provided with and detects hole 6-3.
Described cyclic water tank device 7 comprises fixed support 7-1, water circulating pump 7-2 and rainhat 7-3, fixed support 7-1 is provided with water circulating pump 7-2, water circulating pump 7-2 is provided with rainhat 7-3, and water circulating pump 7-2 links to each other with cyclic water tank device 7 and Venturi tube 5 with valve by pipe.
Described second airduct 8 is provided with the second access hole 8-1, and the water injector in second airduct 8 links to each other with cyclic water tank device 7 with valve by pipe.
Venturi tube 5 in this specific embodiment is to allow between the gas of entrained solids particle and the wash liquid a bigger speed difference be arranged, and allows the particle energy improve, and overcomes hydrophobicity, can throw in the liquid; The latter rotates gas in the moistening cylindrical cavity of periphery, secondary flow many times makes the gas-liquid contact-making surface upgrade with high speed, catches the solid particle that does not enter in the water, and gas-liquid separation under strong centrifugal action, gas rises from central tube at last, outside pipeline is discharged tower; Dusty gas enters first airduct 3 under the strong promotion of centrifugal blower 2, gas speed increases suddenly to more than the 50m/s when collapsible tube 5-3, and this strand high velocity air impacts from the recirculated water of water injector (nozzle) ejection and makes it atomizing, and this promptly is the foam process.Speed was the highest when air-flow reached trunnion 5-4, when high velocity air and drip group clamp-on trunnion 5-4, gas-liquid two-phase fully collides contact, harmful substance in the drop cohesion waste gas, this promptly is a coacervation process, at this, again because gas-liquid has a speed difference, this speed difference is smashed drop and is torn, and has strengthened gas-liquid contact area and flocculating result widely, and this powerful active force makes that the hydrophobicity of harmful components is overcome fully in the waste gas.The pollutant that can be dissolved in liquid also enters among the drop.At convergent divergent channel 5-1, air-flow gradually falls, and static pressure obtains certain recovery, and when incision second airduct 8, speed is reduced to the required speed that enters cyclone separator 6.
Owing to carry a large amount of liquid secretly in the gas, inner surface at cyclone separator 6 forms the complete liquid film of one deck, tangent line and the gas-liquid of going into are descended along spiral inner wall, liquid is then owing to the severe relation is got rid of on inwall, each particle of air-flow is near inwall during helical flow, be not that curve flows, but refraction is flowed many times, be infinite a plurality of " secondary flow " this just make each particle in the gas that the chance that contacts repeatedly with the inwall liquid film is all arranged, be that each solid particle and DDGS all are unable to escape the result who " is caught " by liquid, like this, remove efficient also just inevitable more than 99.8%, separated gas that must be cleaner, the atmosphere that enters up to standard from central tube 6-1 at last.
The advantage of this specific embodiment is: its can improve exhaust-gas treatment economical, stable, efficiently, reduces significantly than conventional process plant area area and weight of equipment and size; Prevent the obstruction of solid particulate matter in the waste gas (comprising the organic class particle that freezes) effectively, thereby reduce the operation cost of factory significantly packing layer or filtration (cloth) layer; The design optimization of central tube gas flow, more help the rotation of gas-liquid-solid three-phase mixture, thereby improve separative efficiency.
Claims (6)
1. whirlwind tower combined exhaust gas treating apparatus, it is characterized in that it is by base plate (1), centrifugal blower (2), first airduct (3), drainpipe (4), Venturi tube (5), cyclone separator (6), cyclic water tank device (7) and second airduct (8) are formed, base plate (1) is provided with centrifugal blower (2), centrifugal blower (2) links to each other with first airduct (3), first airduct (3) links to each other with Venturi tube (5), Venturi tube (5) links to each other with second airduct (8), second airduct (8) links to each other with cyclone separator (6), cyclic water tank device (7) links to each other with the bottom of cyclone separator (6), first airduct (3) links to each other with cyclic water tank device (7) by drainpipe (4), and the water injector in the Venturi tube (5) links to each other with cyclic water tank device (7) with valve by pipe.
2. whirlwind tower combined exhaust gas treating apparatus according to claim 1, it is characterized in that described first airduct (3) comprises first access hole (3-1) and water fender (3-2), first access hole (3-1) is arranged on the afterbody top of first airduct (3), and water fender (3-2) is arranged on the afterbody below inwall of first airduct (3).
3. whirlwind tower combined exhaust gas treating apparatus according to claim 1, it is characterized in that described Venturi tube (5) comprises collapsible tube (5-1), trunnion (5-2) and convergent divergent channel (5-3), one end of collapsible tube (5-1) links to each other with first airduct (3), the other end links to each other with trunnion (5-2), trunnion (5-2) links to each other with convergent divergent channel (5-3), and convergent divergent channel (5-3) links to each other with second airduct (8).
4. whirlwind tower combined exhaust gas treating apparatus according to claim 1, it is characterized in that described cyclone separator (6) comprises central tube (6-1), bypass pipe (6-2) and detects hole (6-3), the arranged outside of cyclone separator (6) has bypass pipe (6-2), central tube (6-1) vertically is vertically set on cyclone separator (6) inside center position, and central tube (6-1) is provided with and detects hole (6-3).
5. whirlwind tower combined exhaust gas treating apparatus according to claim 1, it is characterized in that described cyclic water tank device (7) comprises fixed support (7-1), water circulating pump (7-2) and rainhat (7-3), fixed support (7-1) is provided with water circulating pump (7-2), water circulating pump (7-2) is provided with rainhat (7-3), and water circulating pump (7-2) links to each other with cyclic water tank device (7) and Venturi tube (5) with valve by pipe.
6. whirlwind tower combined exhaust gas treating apparatus according to claim 1 is characterized in that described second airduct (8) is provided with second access hole (8-1), and the water injector in second airduct (8) links to each other with cyclic water tank device (7) with valve by pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201020501340XU CN201799202U (en) | 2010-08-24 | 2010-08-24 | Combined waste gas treatment device of tornado tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201020501340XU CN201799202U (en) | 2010-08-24 | 2010-08-24 | Combined waste gas treatment device of tornado tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201799202U true CN201799202U (en) | 2011-04-20 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201020501340XU Expired - Fee Related CN201799202U (en) | 2010-08-24 | 2010-08-24 | Combined waste gas treatment device of tornado tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201799202U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103349896A (en) * | 2013-07-04 | 2013-10-16 | 大连佳林设备制造有限公司 | Large-scale equipment for filtering air odor and pollutant |
| KR101925745B1 (en) * | 2018-03-09 | 2018-12-05 | 성창호 | A dust collecting device |
| CN110448983A (en) * | 2019-04-09 | 2019-11-15 | 中国电器科学研究院股份有限公司 | It is a kind of for removing the hybrid cleaner of coating cloud in lacquer spraying waste gas |
-
2010
- 2010-08-24 CN CN201020501340XU patent/CN201799202U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103349896A (en) * | 2013-07-04 | 2013-10-16 | 大连佳林设备制造有限公司 | Large-scale equipment for filtering air odor and pollutant |
| KR101925745B1 (en) * | 2018-03-09 | 2018-12-05 | 성창호 | A dust collecting device |
| WO2019172720A1 (en) * | 2018-03-09 | 2019-09-12 | 성창호 | Dust-collecting device |
| CN110448983A (en) * | 2019-04-09 | 2019-11-15 | 中国电器科学研究院股份有限公司 | It is a kind of for removing the hybrid cleaner of coating cloud in lacquer spraying waste gas |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110420 Termination date: 20120824 |