CN201295589Y - Rotating atomization spray tower - Google Patents

Rotating atomization spray tower Download PDF

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Publication number
CN201295589Y
CN201295589Y CNU2008201378402U CN200820137840U CN201295589Y CN 201295589 Y CN201295589 Y CN 201295589Y CN U2008201378402 U CNU2008201378402 U CN U2008201378402U CN 200820137840 U CN200820137840 U CN 200820137840U CN 201295589 Y CN201295589 Y CN 201295589Y
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CN
China
Prior art keywords
tower
tower body
water
waste gas
gas
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
Application number
CNU2008201378402U
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Chinese (zh)
Inventor
张海兵
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Individual
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Individual
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Publication date
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Priority to CNU2008201378402U priority Critical patent/CN201295589Y/en
Application granted granted Critical
Publication of CN201295589Y publication Critical patent/CN201295589Y/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model relates to a rotating atomization spray tower, in particular to a purification device for waste gas generated during recovery processing of waste tires, comprising a tower body, a waste gas transfer pipe and a fan. A gas vent is arranged on the top of the tower body. An inner wall jacket is fixed in the tower body. A rotating atomization nozzle is installed respectively on the top of the inner wall jacket and at the bottom of the inner wall jacket. A water inlet is installed at the tower side which is at the same place as the rotating atomization nozzle. Alkaline liquid is filled in the bottom of the tower body. A liquid level gauge, a drain, a water balance port, a water outlet, an observation port and an oil leakage port are installed at the tower side. A water transmission pipe is installed between the water outlet and the water inlet. The utility model has the advantages of small investment, low operation cost, high recovery and utilization ratio and good waste gas purification effect. The hazardous gas contacts with the alkaline liquid for two times and the alkaline liquid is rotated, atomized and spayed out, thus ensuring full mixing between the alkaline liquid and the hazardous gas and greatly improving the purification efficiency of hazardous gas.

Description

Rotary atomization spray tower
Technical field
The utility model relates to a kind of damaged tire and reclaims processing unit (plant), relates in particular to a kind of to waste gas produced purifier in the damaged tire recovery process.
Background technology
In the recovery process of damaged tire, scrap rubber desulfurization meeting produces a large amount of foul gas, contains moisture in these gases, and a small amount of rubber powder granule is arranged, pernicious gases such as carbon dioxide, hydrogen sulfide, and harmful substances such as benzene, dimethylbenzene.General these [s are known from experience in process of manufacture, are produced by the worksheet heat of looking unfamiliar, and directly are discharged into then in the atmosphere, and amorphous like this discharging waste gas can cause environmental pollution, is unfavorable for environmental protection.At the foul gas that is produced, people wish to have a kind of device simple to operate, that reclaiming clean is effective to purify the waste gas that is produced in the damaged tire recovery process.
Summary of the invention
The utility model is at the problems referred to above, a kind of rotary atomization spray tower is provided,, will reclaims in the process at damaged tire by adopting negative pressure wind, be adsorbed in the rotary atomization spray tower atomizing cooling by the worksheet thermogenetic pernicious gas of looking unfamiliar, uncontrollable discharge is become discharging in a organized way.
The utility model is achieved by the following technical programs, a kind of rotary atomization spray tower, by tower body, the waste gas dispatch tube, blower fan constitutes, waste gas dispatch tube one end stretches into tower body top, the other end connects blower fan, wherein, tower body is by gas vent, the inwall chuck, the rotary-atomizing shower nozzle, water inlet, liquid level gauge, sewage draining exit, the water balance mouth, water out, peep hole, oil leakaging port, the water transfer tube constitutes, the tower body top has gas vent, the waste gas dispatch tube place of stretching into is installed with an inwall chuck in the tower body, these inwall chuck five face closures, open wide below, inwall chuck top and bottom are separately installed with the rotary-atomizing shower nozzle, with the tower side of rotary-atomizing shower nozzle same area water inlet are installed; The tower body bottom fills the akaline liquid that absorbs pernicious gas, and liquid level gauge is installed in the tower side, the tower side bottom is separately installed with sewage draining exit, water balance mouth, water out, tower side on the akaline liquid surface is separately installed with peep hole and oil leakaging port, and the water transfer tube is installed between tower side water out and water inlet.
Operation principle of the present utility model is: the water transfer tube is sent to water inlet with the akaline liquid of tower body bottom from water out, by the rotary-atomizing shower nozzle akaline liquid atomizing is sprayed then.The pernicious gas that the negative pressure that is produced by blower fan produces the shopwork surface is adsorbed to the waste gas dispatch tube and enters the inwall chuck that tower body is come tower body rapidly, pernicious gas is twice akaline liquid through the ejection of rotary-atomizing shower nozzle respectively, harmful substance in the gas by with atomizing after the most of oily mater that generates in akaline liquid reaction back, float over the akaline liquid surface, fraction is dissolved in akaline liquid, reacted gas pours tower body, after running into the akaline liquid surface, rebound, go out tower body from gas vent along the tower wall.Can see from peep hole, when akaline liquid surface oily mater is too much, open oil leakaging port, surperficial oily mater is discharged, replenish akaline liquid from the water balance mouth again, make the utilization of alkalies physical efficiency repetitive cycling, can measure the volume of akaline liquid in the tower body from liquid level gauge, after akaline liquid clean-up effect in the tower body descends, can akaline liquid be discharged from sewage draining exit.
The beneficial effects of the utility model are: this device has characteristics such as small investment, operating cost is low, recovery utilization rate is high, waste gas purification is effective, by twice of pernicious gas contacted with akaline liquid, and the akaline liquid rotary-atomizing sprayed, akaline liquid is fully mixed with pernicious gas, improved the cleaning harmful gas rate greatly.
Description of drawings
Fig. 1 is the utility model structural representation
Among the figure, 1 tower body, 2 waste gas dispatch tubes, 3 blower fans, 4 gas vents, 5 inwall chucks, 6 rotary-atomizing shower nozzles, 7 water inlets, 8 liquid level gauges, 9 sewage draining exits, 10 water balance mouths, 11 water outs, 12 peep holes, 13 oil leakaging ports, 14 water transfer tubes.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is further described:
A kind of rotary atomization spray tower, by tower body 1, waste gas dispatch tube 2, blower fan 3 constitutes, waste gas dispatch tube 2 one ends stretch into tower body 1 top, the other end connects blower fan 3, wherein, tower body 1 is by gas vent 4, inwall chuck 5, rotary-atomizing shower nozzle 6, water inlet 7, liquid level gauge 8, sewage draining exit 9, water balance mouth 10, water out 11, peep hole 12, oil leakaging port 13, water transfer tube 14 constitutes, tower body 1 top has gas vent 4, waste gas dispatch tube 2 places of stretching into are installed with an inwall chuck 5 in the tower body 1, these inwall chuck 5 five face closures, open wide below, inwall chuck 5 tops and bottom are separately installed with rotary-atomizing shower nozzle 6, with the tower side of rotary-atomizing shower nozzle 6 same area water inlet 7 are installed; Tower body 1 bottom fills the akaline liquid that absorbs pernicious gas, and liquid level gauge 8 is installed in the tower side, the tower side bottom is separately installed with sewage draining exit 9, water balance mouth 10, water out 11, tower side on the akaline liquid surface is separately installed with peep hole 12 and oil leakaging port 13, at tower side water out 11 and 7 of water inlets water transfer tube 14 is installed.
Water transfer tube 14 is sent to water inlet 7 with the akaline liquid of tower body 1 bottom from water out 11, by rotary-atomizing shower nozzle 6 the akaline liquid atomizing is sprayed then.The pernicious gas that the negative pressure that is produced by blower fan 3 produces the shopwork surface is adsorbed to waste gas dispatch tube 2 and enters the inwall chuck 5 that tower body 1 is come tower body 1 rapidly, pernicious gas is twice akaline liquid through 6 ejections of rotary-atomizing shower nozzle respectively, harmful substance in the gas by with atomizing after the most of oily mater that generates in akaline liquid reaction back, float over the akaline liquid surface, fraction is dissolved in akaline liquid, all the other unreacted gases pour tower body 1, rebound after running into the akaline liquid surface, 4 go out tower body 1 along the tower wall from gas vent.Can see from peep hole 12, when akaline liquid surface oily mater is too much, open oil leakaging port 13, surperficial oily mater is discharged, replenish akaline liquid from water balance mouth 10 again, make the utilization of alkalies physical efficiency repetitive cycling, can measure the volume of akaline liquid in the tower body 1 from liquid level gauge 8, after akaline liquid clean-up effect in the tower body 1 descends, can akaline liquid be discharged from sewage draining exit 9.

Claims (1)

1, a kind of rotary atomization spray tower, by tower body (1), waste gas dispatch tube (2), blower fan (3) constitutes, waste gas dispatch tube (2) one ends stretch into tower body (1) top, the other end connects blower fan (3), it is characterized in that: tower body (1) is by gas vent (4), inwall chuck (5), rotary-atomizing shower nozzle (6), water inlet (7), liquid level gauge (8), sewage draining exit (9), water balance mouth (10), water out (11), peep hole (12), oil leakaging port (13), water transfer tube (14) constitutes, tower body (1) top has gas vent (4), the interior waste gas dispatch tube of tower body (1) (2) place of stretching into is installed with an inwall chuck (5), these inwall chuck (5) five face closures, open wide below, inwall chuck (5) top and bottom are separately installed with rotary-atomizing shower nozzle (6), with the tower side of rotary-atomizing shower nozzle (6) same area water inlet (7) are installed; Tower body (1) bottom fills the akaline liquid that absorbs pernicious gas, and liquid level gauge (8) is installed in the tower side, the tower side bottom is separately installed with sewage draining exit (9), water balance mouth (10), water out (11), tower side on the akaline liquid surface is separately installed with peep hole (12) and oil leakaging port (13), between tower side water out (11) and water inlet (7) water transfer tube (14) is installed.
CNU2008201378402U 2008-10-30 2008-10-30 Rotating atomization spray tower Expired - Lifetime CN201295589Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008201378402U CN201295589Y (en) 2008-10-30 2008-10-30 Rotating atomization spray tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008201378402U CN201295589Y (en) 2008-10-30 2008-10-30 Rotating atomization spray tower

Publications (1)

Publication Number Publication Date
CN201295589Y true CN201295589Y (en) 2009-08-26

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Application Number Title Priority Date Filing Date
CNU2008201378402U Expired - Lifetime CN201295589Y (en) 2008-10-30 2008-10-30 Rotating atomization spray tower

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CN (1) CN201295589Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101721887B (en) * 2008-10-30 2012-02-01 张海兵 Rotary atomization spray tower
CN107696695A (en) * 2017-10-25 2018-02-16 浙江伟博包装印刷品有限公司 A kind of printing machine

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101721887B (en) * 2008-10-30 2012-02-01 张海兵 Rotary atomization spray tower
CN107696695A (en) * 2017-10-25 2018-02-16 浙江伟博包装印刷品有限公司 A kind of printing machine

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20090826

Effective date of abandoning: 20081030