CN204735069U - Leading treater of wet -type - Google Patents
Leading treater of wet -type Download PDFInfo
- Publication number
- CN204735069U CN204735069U CN201520033508.1U CN201520033508U CN204735069U CN 204735069 U CN204735069 U CN 204735069U CN 201520033508 U CN201520033508 U CN 201520033508U CN 204735069 U CN204735069 U CN 204735069U
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- Prior art keywords
- fluidization tower
- spray equipment
- gas
- device body
- waste
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- Treating Waste Gases (AREA)
Abstract
The utility model discloses a leading treater of wet -type, including device body, water pump, control assembly, spray set, interior fluid cylinder, whirl board, filter equipment, outer fluid cylinder, funnel, garbage bin, interior fluid cylinder is being kept away from the one end of device body has been offered one and has been used for the process clean air after spray set handles carries out the exhaust discharge port, the last sunction inlet that is used for sucking waste gas or useless dirt of offering of spray set, outer fluid cylinder with interior fluid cylinder is kept away from spray set one end is installed together, it is used for carrying out the exhaust outlet with the waste water that the dustiness is little to offer one on the outer fluid cylinder, the outlet with filter equipment's input port connection together, this leading treater of wet -type has improved exhaust -gas treatment efficiency, has improved the gas conditioning cleanliness factor, to effectual, the deodorization of explosive dust disposal, remove the peculiar smell, reduce waste, the installation and maintenance of being convenient for of water resource.
Description
Technical field
The utility model relates to technical field of environment protection equipment, particularly relates to a kind of wet type preprocessor.
Background technology
Along with widely using of wet type preprocessor, traditional wet type preprocessor filter efficiency is not very high, and processed flue gas, dust-like mass treatment are limited.The exchange rate of gas and solution is too fast, capacity of decomposition and chemical synthesis efficiency low, especially inapplicable for VOCs treatment, not obvious for bioxin treatment effect, dangerous class dust should not be collected, gas humidity after process is excessive, adopt semidry method process, need with adsorbent, moisture to be sopped up, excessive to consumptive material use amount, outfit of equipment floor space is large, and installation and transportation are inconvenient.
Therefore, those skilled in the art be devoted to research and develop always a kind ofly improve exhaust treatment efficiency, improve gas treatment cleanliness factor, deodorizing good to explosive dust treatment effect, the water resource that eliminates the unusual smell, reduces waste, be convenient to the wet type preprocessor of installation and maintenance.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of wet type preprocessor, this wet type preprocessor improves exhaust treatment efficiency, improves gas treatment cleanliness factor, deodorizing good to explosive dust treatment effect, the water resource that eliminates the unusual smell, reduces waste, be convenient to installation and maintenance.
For solving the problems of the technologies described above, the wet type preprocessor that the utility model provides, comprise device body, be installed in the water pump on described device body, be installed in the Control Component on described device body, for the spray equipment processed waste gas and useless dirt, for carrying out fluidization tower in rotating discharge to the gas after spray equipment process, the spiral board for deviating from the moisture of the waste gas after spray equipment process be assembled together with described interior fluidization tower, be installed in the many-sided ball for carrying out flow-disturbing to the waste water deviate from spiral board, for the filter of filtration treatment processed waste water, be installed in the outer fluidization tower for waste water to be delivered to filter from spiral board on described device body, be installed in the funnel at described outflow column outlet place, the dustbin for waste particles thing through outer fluidization tower be separated after collect corresponding with described funnel, described interior fluidization tower is through the upper and lower end face of described spray equipment, described interior fluidization tower offers an outlet for being carried out discharging by the pure air after described spray equipment process in the one end away from described device body, described spray equipment offers one for sucking the suction inlet of waste gas or useless dirt, together with described outer fluidization tower and described interior fluidization tower are installed in away from described spray equipment one end, described outer fluidization tower offers a discharge outlet for being carried out discharging by waste water little for dustiness, the input port of described discharge outlet and described filter links together, described water pump and outer fluidization tower are linked together by water pipe, described Control Component and described water pump are electrically connected.
Preferably, described wet type preprocessor also comprises the pool construction for carrying out filtering-depositing and clarification to the waste water after described filtration devices, the pond that described pool construction can allow the water after filtering carry out recycling by three roads forms, and described water pump and described pond are linked together by water pipe.
Preferably, the gas-liquid ratio of described spray equipment and spiral board is 1:5, and gas-liquid exchange rate is at below 1m/s.
Preferably, described wet type preprocessor also comprises frequency converter and the temperature sensor for the controlling described pump rotary speed that are installed on described device body.
After adopting said structure, waste gas and waste water are from suction inlet pre-procesor inside, pump operation is processed waste gas or useless dirt by spray equipment, waste gas after process deviates from portion of water by spiral board, flow-disturbing is carried out by many-sided ball, slow down current and gas currency, extend gas-liquid swap time, gas-liquid ratio is designed to 1:5, exchange rate design is at below 1m/s, gas after process by interior fluidization tower to get rid of from the form of revolving from 1 outlet, waste particles nitride layer after process falls in dustbin by funnel, the ionized layers that dustiness is little enters filter by discharge outlet, fine particle thing is stranded in filter inside, water enters water pump by pond precipitation and recycles, the advantage of this wet type preprocessor is:
1, exhaust-gas treatment exchange rate is lower than like product, improves the treatment effeciency of waste gas;
2, adopt interior fluidization tower design, reduce the humidity of emission gases, can coordinate with precipitron and do half dry type process, improve gas treatment cleanliness factor;
3, this pre-procesor adopts funnel+dustbin design, under the non-stop-machine state of equipment, also can clear up rubbish, better to explosive dust treatment effect;
4, have obvious inhibitory action for bioxin that incinerator produces, electrical control adopts full Based Intelligent Control, by the rotating speed of temperature sensor and Frequency Converter Control water pump, prevents the secondary in processing procedure of the waste gas after burning from producing bioxin;
5, pond is with reference to wastewater treatment mode, designs three independent ponds by filtering, precipitating, overflow the waste recycling and reduce water resource;
6, structure adopts combined type design, is convenient to installation and maintenance.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model wet type preprocessor.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein only for explaining the utility model, and be not used in restriction the utility model.
Refer to Fig. 1, Fig. 1 is the structural representation of the utility model wet type preprocessor.
In the present embodiment, wet type preprocessor 10, comprise device body 20, be installed in the water pump 19 on device body 20, be installed in the Control Component 15 on device body 20, for the spray equipment 11 processed waste gas and useless dirt, for carrying out fluidization tower 12 in rotating discharge to the gas after spray equipment 11 processes, the spiral board 13 for deviating from the moisture of the waste gas after spray equipment 11 processes be assembled together with interior fluidization tower 12, be installed in the many-sided ball for carrying out flow-disturbing to the waste water deviate from spiral board 13, for carrying out the filter 18 of filtration treatment to waste water, be installed in the outer fluidization tower for waste water to be delivered to filter 18 from spiral board 13 on device body 20, be installed in the funnel 21 in outer fluidization tower 14 exit, the dustbin 17 for waste particles thing through outer fluidization tower be separated after collect corresponding with funnel 21, interior fluidization tower 12 is through the upper and lower end face of spray equipment 11, interior fluidization tower 12 offers an outlet for being carried out discharging by the pure air after spray equipment 11 processes in the one end away from device body 20, spray equipment 11 offers one for sucking the suction inlet 111 of waste gas or useless dirt, together with outer fluidization tower 14 and interior fluidization tower 12 are installed in away from described spray equipment 11 one end, outer fluidization tower 14 offers a discharge outlet for being carried out discharging by waste water little for dustiness, the input port of discharge outlet and filter 18 links together, water pump 19 and outer fluidization tower 14 are linked together by water pipe, Control Component 15 and water pump 19 are electrically connected.
Wet type preprocessor 10 also comprises the pool construction 16 for carrying out filtering-depositing and clarification to the waste water after described filtration devices, the pond that pool construction 16 can allow the water after filtering carry out recycling by three roads forms, and described water pump and described pond are linked together by water pipe.
The gas-liquid ratio of spray equipment 11 and spiral board 13 is 1:5, and gas-liquid exchange rate is at below 1m/s.
Outer fluidization tower 14 also offers one for observing the spot check mouth 141 of the working condition of described outflow internal structure.
Wet type preprocessor 10 also comprises frequency converter and the temperature sensor for the controlling described pump rotary speed that are installed on described device body 20.
The workflow of this wet type preprocessor 10 is: waste gas and waste water are from suction inlet pre-procesor inside, water pump 19 runs through spray equipment 11 pairs of waste gas or useless dirt processes, waste gas after process deviates from portion of water by spiral board 13, flow-disturbing is carried out by many-sided ball, slow down current and gas currency, extend gas-liquid swap time, gas-liquid ratio is designed to 1:5, exchange rate design is at below 1m/s, gas after process by interior fluidization tower to get rid of from the form of revolving from outlet 121, waste particles nitride layer after process falls in dustbin 17 by funnel, the ionized layers that dustiness is little enters filter by discharge outlet, fine particle thing is stranded in filter inside, water enters water pump by pond precipitation and recycles, this wet type preprocessor improves exhaust treatment efficiency, improve gas treatment cleanliness factor, good to explosive dust treatment effect, deodorizing, eliminate the unusual smell, reduce the waste of water resource, be convenient to installation and maintenance.
Should be understood that; these are only preferred embodiment of the present utility model; can not therefore limit the scope of the claims of the present utility model; every utilize the utility model description and accompanying drawing content to do equivalent structure or equivalent flow process conversion; or be directly or indirectly used in other relevant technical fields, be all in like manner included in scope of patent protection of the present utility model.
Claims (5)
1. a wet type preprocessor, it is characterized in that: comprise device body, be installed in the water pump on described device body, be installed in the Control Component on described device body, for the spray equipment processed waste gas and useless dirt, for carrying out fluidization tower in rotating discharge to the gas after spray equipment process, the spiral board for deviating from the moisture of the waste gas after spray equipment process be assembled together with described interior fluidization tower, be installed in the many-sided ball for carrying out flow-disturbing to the waste water deviate from spiral board, for carrying out the filter of filtration treatment to waste water, be installed in the outer fluidization tower for waste water to be delivered to filter from spiral board on described device body, be installed in the funnel at described outflow column outlet place, the dustbin for waste particles thing through outer fluidization tower be separated after collect corresponding with described funnel, described interior fluidization tower is through the upper and lower end face of described spray equipment, described interior fluidization tower offers an outlet for being carried out discharging by the pure air after described spray equipment process in the one end away from described device body, described spray equipment offers one for sucking the suction inlet of waste gas or useless dirt, together with described outer fluidization tower and described interior fluidization tower are installed in away from described spray equipment one end, described outer fluidization tower offers a discharge outlet for being carried out discharging by waste water little for dustiness, the input port of described discharge outlet and described filter links together, described water pump and outer fluidization tower are linked together by water pipe, described Control Component and described water pump are electrically connected.
2. wet type preprocessor according to claim 1, it is characterized in that: described wet type preprocessor also comprises the pool construction for carrying out filtering-depositing and clarification to the waste water after described filtration devices, the pond that described pool construction can allow the water after filtering carry out recycling by three roads forms, and described water pump and described pond are linked together by water pipe.
3. wet type preprocessor according to claim 1, is characterized in that: described outer fluidization tower also offers one for observing the spot check mouth of the working condition of described outflow internal structure.
4. wet type preprocessor according to claim 1, is characterized in that: the gas-liquid ratio of described spray equipment and spiral board is 1:5, and gas-liquid exchange rate is at below 1m/s.
5. wet type preprocessor according to claim 1, is characterized in that: described wet type preprocessor also comprises frequency converter and the temperature sensor for the controlling described pump rotary speed that are installed on described device body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520033508.1U CN204735069U (en) | 2015-01-16 | 2015-01-16 | Leading treater of wet -type |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520033508.1U CN204735069U (en) | 2015-01-16 | 2015-01-16 | Leading treater of wet -type |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204735069U true CN204735069U (en) | 2015-11-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520033508.1U Expired - Fee Related CN204735069U (en) | 2015-01-16 | 2015-01-16 | Leading treater of wet -type |
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| Country | Link |
|---|---|
| CN (1) | CN204735069U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106976929A (en) * | 2017-04-21 | 2017-07-25 | 徐州工程学院 | A kind of sewage solid granulates removal device |
-
2015
- 2015-01-16 CN CN201520033508.1U patent/CN204735069U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106976929A (en) * | 2017-04-21 | 2017-07-25 | 徐州工程学院 | A kind of sewage solid granulates removal device |
| CN106976929B (en) * | 2017-04-21 | 2020-10-20 | 徐州工程学院 | Solid-state granule remove device of sewage |
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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 |
Granted publication date: 20151104 Termination date: 20180116 |
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| CF01 | Termination of patent right due to non-payment of annual fee |