CN206566743U - A kind of foul waste gas processing unit - Google Patents
A kind of foul waste gas processing unit Download PDFInfo
- Publication number
- CN206566743U CN206566743U CN201720208778.0U CN201720208778U CN206566743U CN 206566743 U CN206566743 U CN 206566743U CN 201720208778 U CN201720208778 U CN 201720208778U CN 206566743 U CN206566743 U CN 206566743U
- Authority
- CN
- China
- Prior art keywords
- tower body
- water
- fenton oxidation
- upper strata
- waste 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 - Fee Related
Links
- 239000002912 waste gas Substances 0.000 title claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 41
- 239000007921 spray Substances 0.000 claims abstract description 28
- 239000000945 filler Substances 0.000 claims abstract description 12
- 239000000126 substance Substances 0.000 claims abstract description 8
- 230000004888 barrier function Effects 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 54
- 230000003647 oxidation Effects 0.000 claims description 36
- 238000007254 oxidation reaction Methods 0.000 claims description 36
- 238000005406 washing Methods 0.000 claims description 30
- 230000008676 import Effects 0.000 claims description 12
- 241000209094 Oryza Species 0.000 claims description 7
- 235000007164 Oryza sativa Nutrition 0.000 claims description 7
- 235000009566 rice Nutrition 0.000 claims description 7
- 239000013618 particulate matter Substances 0.000 claims description 5
- 238000002347 injection Methods 0.000 claims description 2
- 239000007924 injection Substances 0.000 claims description 2
- 239000000243 solution Substances 0.000 claims description 2
- 239000007789 gas Substances 0.000 abstract description 19
- 238000010276 construction Methods 0.000 abstract description 4
- 231100000614 poison Toxicity 0.000 abstract description 3
- 230000007096 poisonous effect Effects 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000009933 burial Methods 0.000 description 1
- 238000002144 chemical decomposition reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 238000010525 oxidative degradation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Abstract
The utility model is related to a kind of foul waste gas processing unit, including settling tank and purifying column, air inlet pipe is installed on the closure of settling tank, escape pipe is also equipped with closure, purifying column bottom side is provided with air intlet, the outlet of escape pipe is connected with air intlet, air outlet slit is provided with the top of purifying column, horizontally disposed dividing plate is provided with the middle part of purifying column, tower body is divided into upper strata tower body and lower floor's tower body by dividing plate, the first spray equipment is provided with the top of the tower body of upper strata, the first filler is installed below the first spray equipment in the tower body of upper strata, the second spray equipment is provided with the top of lower floor's tower body, the breather line for connecting upper strata tower body with lower floor tower body is provided with dividing plate, the baffle plate entered for barrier liquid in breather line is fixed with below first filler.The utility model can purify the poisonous and harmful substance carried in gas totally, reach gas discharging standards, and whole device is simple in construction, small volume, safe and convenient to use, low cost, be easy to promote.
Description
Technical field
The utility model is related to a kind of waste gas treatment equipment, and in particular to a kind of foul waste gas processing unit.
Background technology
China is that garbage-surrounded city is general to use at the techniques such as burial, burning, chemical degradation than more serious country in the world
Reason, and substantial amounts of poisonous flavored foul gas can be produced in garbage processing procedure, it brings to the healthy of resident
High risks, the processing to foul gas at present is typically diluted using large scale equipment to gas, chemical absorbing etc., current institute
Complicated with device structure, volume ratio is larger, is awkward.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of foul waste gas processing unit, and it can handle waste gas
In noxious material and dust, gas qualified discharge can be realized, and simple in construction, cost is low.
To achieve the above object, the technical scheme that the utility model is taken is:
A kind of foul waste gas processing unit, including settling tank and purifying column, settling tank is built with for except particulate matter and water
The running water of soluble substance, settling tank port, which is provided with, is provided with deeply entering below originally water level on closure, closure
It is equipped with tracheae, air inlet pipe on air blower, closure and is also equipped with escape pipe, the import of escape pipe is located in originally water level
Side, purifying column bottom side is provided with air intlet, and the outlet of escape pipe is connected with air intlet, is set at the top of purifying column
Have to be connected with discharge duct, discharge duct on air outlet slit, air outlet slit and silk screen dehydrater is installed, be provided with the middle part of purifying column
Tower body is divided at the top of upper strata tower body and lower floor's tower body, upper strata tower body and is provided with to enter with washings by horizontally disposed dividing plate, dividing plate
The first filler, upper strata tower body bottom are installed below the first spray equipment in first spray equipment of mouth connection, upper strata tower body
The the second spray dress for being provided with and being connected with Fenton oxidation liquid import at the top of washing water out, lower floor's tower body is provided with the wall of side
Put, the second filler is installed in the second spray equipment in lower floor's tower body, lower floor's tower body bottom is provided with Fenton oxidation liquid outlet, institute
State and be fixed with below the breather line for being provided with dividing plate and connecting upper strata tower body with lower floor tower body, the first filler for stopping liquid
The baffle plate that body enters in breather line.
First spray equipment includes being connected to the first water main on washing water inlet, and the first water main end is connected with
In the first playpipe of rice font shape, jet is evenly equipped with the first playpipe.
The washing water inlet is connected with washings water inlet pipe, and washings water inlet pipe is connected with washing water collecting groove, is washed
First water pump is installed, washing water out is connected by pipeline with washing water collecting groove on water water inlet pipe.
Second spray equipment includes the second water main being connected in Fenton oxidation liquid import, the second water main end
It is connected with the second playpipe in rice font shape, the second playpipe and is evenly equipped with jet.
The Fenton oxidation liquid import is connected with Fenton oxidation liquid inlet pipe, and Fenton oxidation liquid inlet pipe is collected with Fenton oxidation liquid
Groove is connected, and the second water pump is provided with Fenton oxidation liquid inlet pipe, and Fenton oxidation liquid outlet is received by pipeline and Fenton oxidation liquid
Collect groove connection.
Four breather lines are uniformly laid on the dividing plate.
The baffle plate is U-shaped, and baffle plate is covered on above breather line.
The utility model is provided with dividing plate in tower body, and the ventilation for connecting upper strata tower body with lower floor tower body is provided with dividing plate
Baffle plate is provided with above pipeline, breather line, can so avoid washings from entering in Fenton oxidation liquid and dilute Fenton oxidation liquid, this
Utility model can be removed the particle in waste gas and water-soluble substances by settling tank, and the gas after processing is entered by escape pipe
Enter lower floor's tower body and fully contacted with the Fenton oxidation liquid that the second spray equipment sprays, the biological drop of the hardly possible in oxidative degradation foul waste gas
Thing is solved, the gas after Fenton oxidation liquid oxidation processing enters upper strata tower body, the injection of the first spray equipment by breather line
Cleaning solution washs the Fenton oxidation liquid carried in gas and the particulate matter do not removed, and then gas is entered by discharge duct
Enter silk screen dehydrater and remove moisture to drain into the poisonous and harmful substance carried in the external world, gas and be cleaned totally, reach national gas
Discharge standard, and whole device is simple in construction, small volume, safe and convenient to use, low cost, is easy to promote.
Brief description of the drawings
Fig. 1 is the utility model structural representation.
Fig. 2 is the utility model the first spray equipment structural representation.
Embodiment
The utility model is described in further detail below in conjunction with the accompanying drawings.
As Figure 1-Figure 2, a kind of foul waste gas processing unit, including settling tank 1 and purifying column 2, settling tank 1 built with
The particulate matter and the running water of water-soluble substances carried for absorbing in gas, settling tank port is provided with closure, closure
On be provided with deep originally below water level air inlet pipe 3, air inlet pipe 3 air blower 4 be housed, air blower can by industrial production or
The waste gas that house refuse is produced is sent in settling tank 1, is entered by air inlet pipe 3 below liquid level, the particulate matter that carries in gas and
Water-soluble substances is absorbed by running water, and escape pipe 5 is also equipped with closure, and the import of escape pipe 5 is located in originally water level
Side, the bottom side of purifying column 2 is provided with air intlet, and the outlet of escape pipe 5 is connected with air intlet, and the top of purifying column 2 is set
Have and discharge duct 6 is connected with air outlet slit, air outlet slit, be provided with discharge duct 6 in the middle part of silk screen dehydrater 7, purifying column
Provided with horizontally disposed dividing plate 8, tower body is divided at the top of upper strata tower body and lower floor's tower body, upper strata tower body and is provided with washing by dividing plate 8
Wash in the first spray equipment 9 of water inlet connection, upper strata tower body and the first filler 10, first are installed below the first spray equipment
Filler 10 enables gas fully to be contacted with washings, and washing water out, lower floor's tower are provided with the tower body bottom end side wall of upper strata
It is provided with the second spray equipment 11 being connected with Fenton oxidation liquid import, lower floor's tower body and is installed in the second spray equipment at the top of body
There is the second filler 12, lower floor's tower body bottom, which is provided with Fenton oxidation liquid outlet, the dividing plate, to be provided with upper strata tower body with
The baffle plate 14 entered for barrier liquid in breather line is fixed with below the breather line 13 of layer tower body connection, the first filler,
Baffle plate is U-shaped, and baffle plate is covered on above breather line, and baffle plate 14 can enter breather line 13 with barrier liquid from breather line upper end
It is interior and do not influence gas to pass through.
First spray equipment 9 includes being connected to the first water main 91 on washing water inlet, and the first water main end is connected with
In the first playpipe 92 of rice font shape, jet is evenly equipped with the first playpipe, the first spray equipment 9 is using rice font shape
First playpipe 92, so sprays uniform, broad covered area, it is ensured that liquid is fully contacted with gas.Second spray equipment 11 and
The structure of one spray equipment 9 is identical, and it includes the second water main being connected in Fenton oxidation liquid import, and the second water main end connects
It is connected on the second playpipe in rice font shape, the second playpipe and is evenly equipped with jet.
Washing water inlet is connected with washings water inlet pipe 15, and washings water inlet pipe 15 is connected with washing water collecting groove 16, is washed
Wash and the first water pump 17 is installed on water water inlet pipe, washing water out is connected by pipeline with washing water collecting groove, such washings
It can be recycled, economize on resources, reduce cost.
The import of Fenton oxidation liquid is connected with Fenton oxidation liquid inlet pipe 18, and Fenton oxidation liquid inlet pipe 18 is collected with Fenton oxidation liquid
Groove 19 is connected, and the second water pump 20 is provided with Fenton oxidation liquid inlet pipe, and Fenton oxidation liquid outlet passes through pipeline and Fenton oxidation
Liquid collecting tank 19 is connected.
The utility model uniformly lays four breather lines on dividing plate, simple in construction, while ensure that gas circulation is smooth,
Improve gas treatment efficiency.
Claims (7)
1. a kind of foul waste gas processing unit, it is characterised in that:Including settling tank and purifying column, settling tank is built with for absorbing
The running water of particulate matter and water-soluble substances, settling tank port, which is provided with closure, closure, is provided with deeply originally aqueous
It is equipped with air inlet pipe below face, air inlet pipe on air blower, closure and is also equipped with escape pipe, the import of escape pipe is located at originally
Above water level, purifying column bottom side is provided with air intlet, and the outlet of escape pipe is connected with air intlet, purifying column
Top, which is provided with air outlet slit, air outlet slit, is connected with discharge duct, and silk screen dehydrater, purifying column are provided with discharge duct
Middle part is provided with horizontally disposed dividing plate, and tower body is divided into upper strata tower body and lower floor's tower body by dividing plate, be provided with the top of the tower body of upper strata with
Wash in the first spray equipment of water inlet connection, upper strata tower body and the first filler, upper strata are installed below the first spray equipment
It is provided with washing water out on tower body bottom end side wall, the be connected with Fenton oxidation liquid import is provided with the top of lower floor's tower body
The second filler is installed in the second spray equipment in two spray equipments, lower floor's tower body, lower floor's tower body bottom is provided with Fenton oxidation liquid
It is provided with below the breather line for connecting upper strata tower body with lower floor tower body, the first filler and is fixed with outlet, the dividing plate
The baffle plate entered for barrier liquid in breather line.
2. foul waste gas processing unit according to claim 1, it is characterised in that:First spray equipment includes connection
The first water main on washing water inlet, the first water main end is connected with the first playpipe in rice font shape, the first injection
Jet is evenly equipped with pipe.
3. foul waste gas processing unit according to claim 2, it is characterised in that:The washing water inlet enters with washings
Water pipe is connected, and washings water inlet pipe is connected with washing water collecting groove, the first water pump is provided with washings water inlet pipe, washings go out
Mouth is connected by pipeline with washing water collecting groove.
4. foul waste gas processing unit according to claim 1, it is characterised in that:Second spray equipment includes connection
The second water main in Fenton oxidation liquid import, the second water main end is connected with the second playpipe in rice font shape, the
Jet is evenly equipped with two playpipes.
5. foul waste gas processing unit according to claim 4, it is characterised in that:The Fenton oxidation liquid import and Fenton
Oxidation solution inlet pipe is connected, and Fenton oxidation liquid inlet pipe is connected with Fenton oxidation liquid collecting tank, and the is provided with Fenton oxidation liquid inlet pipe
Two water pumps, Fenton oxidation liquid outlet is connected by pipeline with Fenton oxidation liquid collecting tank.
6. foul waste gas processing unit according to claim 1, it is characterised in that:Uniform laying four is led on the dividing plate
Feed channel.
7. foul waste gas processing unit according to claim 1, it is characterised in that:The baffle plate is U-shaped, and baffle plate covers on logical
Above feed channel.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720208778.0U CN206566743U (en) | 2017-03-06 | 2017-03-06 | A kind of foul waste gas processing unit |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720208778.0U CN206566743U (en) | 2017-03-06 | 2017-03-06 | A kind of foul waste gas processing unit |
Publications (1)
Publication Number | Publication Date |
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CN206566743U true CN206566743U (en) | 2017-10-20 |
Family
ID=60056333
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720208778.0U Expired - Fee Related CN206566743U (en) | 2017-03-06 | 2017-03-06 | A kind of foul waste gas processing unit |
Country Status (1)
Country | Link |
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CN (1) | CN206566743U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108543393A (en) * | 2018-06-06 | 2018-09-18 | 盐城旭恒环保科技有限公司 | A kind of casting exhaust gas acid mist purifying tower |
CN108671681A (en) * | 2018-06-11 | 2018-10-19 | 滨海金海立医药化工有限公司 | A kind of cyclopropyl carboxylic acid synthesis waste gas collection device |
-
2017
- 2017-03-06 CN CN201720208778.0U patent/CN206566743U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108543393A (en) * | 2018-06-06 | 2018-09-18 | 盐城旭恒环保科技有限公司 | A kind of casting exhaust gas acid mist purifying tower |
CN108671681A (en) * | 2018-06-11 | 2018-10-19 | 滨海金海立医药化工有限公司 | A kind of cyclopropyl carboxylic acid synthesis waste gas collection device |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171020 |
|
CF01 | Termination of patent right due to non-payment of annual fee |