CN109731459A - Gas pollutant processor - Google Patents
Gas pollutant processor Download PDFInfo
- Publication number
- CN109731459A CN109731459A CN201910173851.9A CN201910173851A CN109731459A CN 109731459 A CN109731459 A CN 109731459A CN 201910173851 A CN201910173851 A CN 201910173851A CN 109731459 A CN109731459 A CN 109731459A
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- CN
- China
- Prior art keywords
- gas
- water tank
- plate
- water
- cabinet
- 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.)
- Pending
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- 239000003344 environmental pollutant Substances 0.000 title claims abstract description 32
- 231100000719 pollutant Toxicity 0.000 title claims abstract description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 86
- 238000001914 filtration Methods 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 13
- 239000007787 solid Substances 0.000 claims abstract description 13
- 238000005367 electrostatic precipitation Methods 0.000 claims abstract description 5
- 239000007789 gas Substances 0.000 claims description 92
- 239000012530 fluid Substances 0.000 claims description 26
- 239000007788 liquid Substances 0.000 claims description 19
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 11
- 239000003546 flue gas Substances 0.000 claims description 11
- 230000001413 cellular effect Effects 0.000 claims description 8
- 239000000523 sample Substances 0.000 claims description 6
- 238000012544 monitoring process Methods 0.000 claims description 2
- 239000000126 substance Substances 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 6
- 239000003500 flue dust Substances 0.000 abstract description 5
- 239000002699 waste material Substances 0.000 abstract description 5
- 238000011084 recovery Methods 0.000 abstract description 3
- 238000004064 recycling Methods 0.000 abstract description 3
- 239000000809 air pollutant Substances 0.000 abstract description 2
- 231100001243 air pollutant Toxicity 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 abstract description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 8
- 239000000428 dust Substances 0.000 description 4
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000004202 carbamide Substances 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000003915 air pollution Methods 0.000 description 2
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 2
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 2
- 235000011130 ammonium sulphate Nutrition 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000012372 quality testing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The invention belongs to flue dust air pollutants processing technology fields, more particularly, to a kind of gas pollutant processor, including filtration system, control system, auxiliary system, filtration system includes water tank processing unit, air intake and exhaust system, cabinet water tank, gas distributor in the air water process layer is set, it is characterized in that, gas distributor includes top layer gas plate, the internal gas plate of N layer of this top layer gas plate lower part is set, every layer of internal gas plate includes solid plate, the spiracular plate being connected with this solid plate, every two layers adjacent inside gas plate reversed arrangement, Separate System of Water-jet is connected with lift pump exhaust outlet, electrostatic precipitation system and vapour lock device are equipped at water tank exhaust pipe, temperature control system and water level control system are connected with cabinet water tank.The configuration of the present invention is simple, high treating effect is easy to maintain, and the pollutant by processing recycling can generate during recovery processing can use substance, turns waste into wealth and generates secondary value, reduces processing cost.
Description
Technical field
The invention belongs to flue dust air pollutants processing technology fields, more particularly, to a kind of gas pollutant processor.
Background technique
At present in the world, the excess emitters of air pollution have seriously affected the quality of life of people and the hair of the mankind
Exhibition, the discharge discharge of control atmosphere pollution air has been pendulum in face of the mankind, and people find out various methods to carry out air pollution
With the processing of heat dissipation, such as dry method, wet process, bag-type dust, moisture film, the methods of desulfurization etc..But effect is all undesirable, and
Some methods are at high cost can not large-area applications.Application No. is 201821151920.3 Chinese patents, and providing one kind can return
It receives heat and handles the scheme of smoke contamination object, solve the above problem substantially, but still remain gas distributor appendix
Not ageing-resistant at work, the halfway problem of gas treatment.
Summary of the invention
The object of the present invention is to provide a kind of simple and reasonable, gas pollutant high treating effect has a wide range of application, if
Standby gas pollutant processor easy to maintain.
The purpose of the present invention is what is realized by following technical proposals:
Gas pollutant processor of the invention, including filtration system, the control system being connected with this filtration system are and described
The auxiliary system that filtration system is connected, the filtration system include water tank processing unit, are connected with this water tank processing unit
The air intake and exhaust system connect, the water tank processing unit include dividing the cabinet of conducting shell containing upper layer air water process layer and lower layer's gas collection
The treatment fluid water inlet and treatment fluid water outlet of this cabinet water tank side is arranged in water tank, is arranged in cabinet water tank lower part
Flue gas air inlet, the gas distributor in the air water process layer is set, one to be connected with this gas distributor bottom
Group is gas-guide tube, and the air intake and exhaust system includes lift pump, and lift pump air inlet and lift pump on this lift pump is arranged in
Exhaust outlet, the water tank exhaust pipe being connected with this lift pump, the lift pump is connected with the control system, described
Auxiliary system includes residual neat recovering system, Electrostatic Control system and pollutant monitoring system,
It is characterized in that, the gas distributor includes top layer gas plate, the internal gas of N layer of this top layer gas plate lower part is set
Plate, every layer of internal gas plate includes solid plate, the spiracular plate being connected with this solid plate, every two layers adjacent inside gas plate reversed arrangement,
The top layer gas plate is equipped with cellular stomata, and the spiracular plate is equipped with cellular stomata,
It is connected with Separate System of Water-jet with the lift pump exhaust outlet, this Separate System of Water-jet includes liquid storage device and gas collection
Device is equipped with vapour lock device at the water tank exhaust pipe, is equipped with electrostatic precipitation system in the inner upper of the liquid storage device,
It is equipped with air inlet on the cabinet water tank top,
The gas-guide tube is straight tube.
Temperature control system and water level control system are connected with the cabinet water tank.
Solid plate area described in the area ratio of the spiracular plate is small.
The temperature control system includes the temperature probe being connected with the cabinet water tank, is connected with this temperature probe
It connects and the temperature controller in master control device is set.
The water level control system includes the water pump being connected with the cabinet water tank, is connected and sets with this water pump
Set the water level controller in master control device.
The cabinet water tank is connected with observation service ports.
Advantages of the present invention:
(1) gas pollutant processor of the invention, has a wide range of application, and structure is simple, high treating effect, easy to maintain, passes through
The pollutant of processing recycling can generate during recovery processing can use substance, turns waste into wealth and generates secondary value, reduces
Processing cost；
(2) gas pollutant processor of the invention, exhaust-gas treatment is more thorough, and exhaust gas is contacted in gas distributor and is chemically treated
The movement of S type is carried out during liquid, runing time is longer, and gas-liquid contact is more thorough, heat absorption more sufficiently；
(3) treatment fluid is evacuated in cabinet by gas pollutant processor of the invention, when work, and liquid level is higher than gas distributor,
Treatment fluid is drained under gas distributor when stopping working, reduces the loss of air inlet pipe, long service life；
(4) gas pollutant processor of the invention, during processing, the substances such as sulfur dioxide and oxynitrides are being handled
It is chemically reacted in water tank, generates the benefit materials such as ammonium sulfate, turn waste into wealth；
(5) present invention can be arranged at smoke exhaust pipe when for oil-burning internal combustion engine processing for gas pollutant processor of the invention
Position, interior storage urea solution for the treatment of box body etc. can eliminate sulfur dioxide, oxynitrides, and the harmful substances such as carbon dust reduce tail
The discharge of gas pollutant purifies air.
Detailed description of the invention
Fig. 1 is the structural diagram of the present invention.
Fig. 2 is the structural schematic diagram of gas distributor of the present invention.
Specific embodiment
A specific embodiment of the invention is further illustrated with reference to the accompanying drawing.
As shown in Figure 1, 2, gas pollutant processor of the invention, including filtration system, are connected with this filtration system
Control system, the auxiliary system being connected with the filtration system, the filtration system includes water tank processing unit, with this
The air intake and exhaust system that water tank processing unit is connected, the water tank processing unit include containing upper layer air water process layer and lower layer
Gas collection divides the cabinet water tank 1 of conducting shell, the treatment fluid water inlet 2 and treatment fluid water outlet 3 of this 1 side of cabinet water tank is arranged in, if
The flue gas air inlet 4 in 1 lower part of cabinet water tank is set, the gas distributor 5 in the air water process layer is set, with this gas
Be connected one group of 5 bottom of body dispenser is gas-guide tube 6, and the air intake and exhaust system includes lift pump 7, is arranged in this lift pump
Lift pump air inlet 8 and lift pump exhaust outlet 9 on 7, the water tank exhaust pipe 10 being connected with this lift pump 7, the air-breathing
Machine 7 is connected with the control system 13, and the auxiliary system includes residual neat recovering system, Electrostatic Control system and pollution
Quality testing examining system,
It is characterized in that, the gas distributor 5 includes top layer gas plate 5-1, the N layer of the lower part this top layer gas plate 5-1 is set
Internal gas plate 5-2, every layer of internal gas plate 5-2 includes solid plate 5-2-1, the spiracular plate 5-2-2 being connected with this solid plate 5-2-1, often
Two layers of adjacent inside gas plate 5-2 reversed arrangement, the top layer gas plate 5-1 are equipped with cellular stomata 14, the stomata
Plate 5-2-2 is equipped with cellular stomata 14,
It is connected with Separate System of Water-jet with the lift pump exhaust outlet 9, this Separate System of Water-jet includes liquid storage device 15 and gas
Collector is equipped with vapour lock device 11 at the water tank exhaust pipe 10, removes in the inner upper of the liquid storage device equipped with electrostatic
Dirt system 12,
It is connected with temperature control system and water level control system with the cabinet water tank 1,
Be equipped with air inlet 20 on 1 top of cabinet water tank, when carry out reducing water level worked when, air inlet at air inlet 20
Valve is opened, and is carried out air inlet, is advantageously reduced negative pressure, carries out reducing water level work,
The gas-guide tube 6 is straight tube, avoids swan-neck and is easy to produce fatigue during continuous stretch bending, and makes to lead
The problem of 6 service life of tracheae shortens.
Solid plate 5-2-1 area described in the area ratio of the spiracular plate 5-2-2 is small.
The temperature control system includes the temperature probe 18 being connected with the cabinet water tank 1, with this temperature probe
18 are connected and the temperature controller 15 in master control device are arranged in.
The water level control system includes the water pump 17 being connected with the cabinet water tank 1, is connected with this water pump 17
It connects and the water level controller 16 in master control device is set.
The cabinet water tank 1 is connected with observation service ports 19.
Gas pollutant processor of the invention is carrying out boiler flue gas pollutant soot emissions improvement and heat utilization
When, control temperature reaches set temperature, when temperature reaches set temperature, is adjusted by control pollution treatment fluid water level height
Contact of the gas distributor with treatment fluid, to achieve the purpose that gas cleaning and UTILIZATION OF VESIDUAL HEAT IN.
When work, it is supplemented in treatment fluid from treatment fluid water inlet 2 to cabinet water tank 1, starts lift pump 7, is opened in lift pump 7
After dynamic, continue to inject treatment fluid, so that treatment fluid liquid level is higher than gas distributor 5, gas distributor 5 is made to be immersed in treatment fluid liquid
It works below face；When needing to stop working, treatment fluid is discharged by treatment fluid water outlet 3, and treatment fluid water level is made to be reduced to gas
Body dispenser 5 is hereinafter, treatment fluid cannot enter combustion chamber or air inlet pipe, and then lift pump 7 stops working.The water for the treatment of fluid
Position is controlled by water level control system.
Gas distributor 5 at work, under the suction function of lift pump 7, the flue dust of boiler and flame is extracted out, flue dust
It into gas distributor 5, is contacted with the treatment fluid in gas distributor 5, generates chemical reaction, flue gas pollutant is by atmosphere
Bubble becomes micro-bubble, is discharged by gas distributor 5, flue dust is filtered.In order to increase flue gas in gas distributor 5
Flowing time, gas distributor 5 is designed to multilayered structure, that is, includes top layer gas plate 5-1, be arranged in this top layer gas by the present invention
The internal gas plate 5-2 of the N layer of the lower part plate 5-1, every layer of internal gas plate 5-2 includes solid plate 5-2-1, is connected with this solid plate 5-2-1
Spiracular plate 5-2-2, every two layers adjacent inside gas plate 5-2 reversed arrangement, top layer gas plate 5-1 are equipped with cellular stomata 14, gas
Orifice plate 5-2-2 is equipped with cellular stomata 14, and flue gas can be made to carry out S type movement in gas distributor 5 in this way, increase cigarette
Flowing time of the gas in gas distributor 5 is realized flue gas with treatment fluid and is come into full contact with, and extends chemical reaction and heat turns
It changes, when reduction moves in liquid because of gas, bubble coalescence expands, and reduces treatment effect.The flue gas handled through treatment fluid is through inhaling
Exhaust apparatus enter Separate System of Water-jet, it can be achieved that gas and remaining liquid separation, remaining liquid enters liquid storage device 15, gas
It can further recycle.
Treatment fluid can be the chemical pretreatment solutions such as water, urea, ammoniacal liquor, lye or biological bacteria according to actual treatment needs
Equal liquid.
On the one hand present invention vapour lock device 11 at water tank exhaust pipe 10, vapour lock device 11 can prevent the coke of untreated flue gas
Oil, dust enter 7 clogging impeller of suction ventilator, on the other hand also excessive moisture can be stopped to enter suction ventilator 7.It is equipped in liquid storage device 15
Electrostatic precipitation system 12 is provided with electrostatic generator in electrostatic precipitation system 12, can carry out dust-proof processing to flue gas.
Gas pollutant processor of the invention, structure is simple, has a wide range of application, and high treating effect is easy to maintain, passes through
The pollutant of processing recycling can generate during recovery processing can use substance, turns waste into wealth and generates secondary value, reduces
Processing cost；Exhaust-gas treatment is more thorough, and exhaust gas carries out the movement of S type, fortune during gas distributor 5 contacts chemical pretreatment solution
The row time is longer, and gas-liquid contact is more thorough, heat absorption more sufficiently；Treatment fluid is evacuated in cabinet water tank 1 when work,
Liquid level is higher than gas distributor 5, drains under gas distributor 5 treatment fluid when stopping working, reduces the loss of air inlet pipe,
Long service life；Gas pollutant processor of the invention, during processing, the substances such as sulfur dioxide and oxynitrides exist
It is chemically reacted in cabinet water tank 1, generates the benefit materials such as ammonium sulfate, turn waste into wealth；Gas pollutant processing of the invention
When for oil-burning internal combustion engine processing, position can be arranged at smoke exhaust pipe, storage urea solution etc. can in treatment box body in the present invention by device
Sulfur dioxide, oxynitrides are eliminated, the harmful substances such as carbon dust reduce the discharge of exhaust pollutant, purify air.
Claims (6)
1. a kind of gas pollutant processor, including filtration system, the control system being connected with this filtration system, with the mistake
The auxiliary system that filter system is connected, the filtration system include water tank processing unit, are connected with this water tank processing unit
Air intake and exhaust system, the water tank processing unit includes dividing the cabinet water of conducting shell containing upper layer air water process layer and lower layer's gas collection
Cabinet is arranged in the treatment fluid water inlet and treatment fluid water outlet of this cabinet water tank side, cabinet water tank lower part is arranged in
The gas distributor in the air water process layer is arranged in flue gas air inlet, one group to be connected with this gas distributor bottom
For gas-guide tube, the air intake and exhaust system includes lift pump, and the lift pump air inlet on this lift pump and lift pump row is arranged in
Port, the water tank exhaust pipe being connected with this lift pump, the lift pump are connected with the control system, and described is auxiliary
Auxiliary system includes residual neat recovering system, Electrostatic Control system and pollutant monitoring system,
It is characterized in that, the gas distributor includes top layer gas plate, the internal gas of N layer of this top layer gas plate lower part is set
Plate, every layer of internal gas plate includes solid plate, the spiracular plate being connected with this solid plate, every two layers adjacent inside gas plate reversed arrangement,
The top layer gas plate is equipped with cellular stomata, and the spiracular plate is equipped with cellular stomata,
It is connected with Separate System of Water-jet with the lift pump exhaust outlet, this Separate System of Water-jet includes liquid storage device and gas collection
Device,
Vapour lock device is equipped at the water tank exhaust pipe,
It is equipped with electrostatic precipitation system in the inner upper of the liquid storage device,
It is equipped with air inlet on the cabinet water tank top,
The gas-guide tube is straight tube.
2. gas pollutant processor according to claim 1, it is characterised in that be connected with temperature with the cabinet water tank
Spend control system and water level control system.
3. gas pollutant processor according to claim 1, it is characterised in that described in the area ratio of the spiracular plate
Solid plate area it is small.
4. gas pollutant processor according to claim 1, it is characterised in that the temperature control system include with
The temperature probe that the cabinet water tank is connected is connected with this temperature probe and the control of the temperature in master control device is arranged in
Device.
5. gas pollutant processor according to claim 1, it is characterised in that the water level control system include with
The water pump that the cabinet water tank is connected is connected with this water pump and the water level controller in master control device is arranged in.
6. gas pollutant processor according to claim 1, it is characterised in that the cabinet water tank is connected with observation
Service ports.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910173851.9A CN109731459A (en) | 2019-03-08 | 2019-03-08 | Gas pollutant processor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910173851.9A CN109731459A (en) | 2019-03-08 | 2019-03-08 | Gas pollutant processor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109731459A true CN109731459A (en) | 2019-05-10 |
Family
ID=66369808
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910173851.9A Pending CN109731459A (en) | 2019-03-08 | 2019-03-08 | Gas pollutant processor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109731459A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110980596A (en) * | 2019-12-18 | 2020-04-10 | 王信荣 | Forklift internal combustion engine cover with cooling and odor removing functions |
| CN111495159A (en) * | 2020-05-29 | 2020-08-07 | 祝恩波 | Processor for automatically adjusting gas pollutant discharge value |
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|---|---|---|---|---|
| BE729053A (en) * | 1968-05-07 | 1969-08-01 | ||
| FR2473493A1 (en) * | 1979-09-28 | 1981-07-17 | Tomenko Viktor | Carbonisation column for sodium hydrogen carbonate prodn. - has perforated plates, overflows and cooling pipes arranged to increase heat and material exchange |
| CN205461674U (en) * | 2016-01-17 | 2016-08-17 | 刘伟华 | Exhaust gases filter tower |
| CN206543510U (en) * | 2017-01-18 | 2017-10-10 | 上海杓玉医药科技有限公司 | A kind of tail gas absorber of phenmethylol production |
| CN207928959U (en) * | 2018-01-19 | 2018-10-02 | 天津浩元精细化工股份有限公司 | A kind of circulated sprinkling tail gas absorber |
| CN108826760A (en) * | 2018-07-23 | 2018-11-16 | 麦克维尔空调制冷(武汉)有限公司 | The multistage flooded evaporator of spiracular plate structure and anti-absorbing gas belt liquid |
| CN108815992A (en) * | 2018-07-20 | 2018-11-16 | 祝恩波 | The air pollutants processor of heat-recoverable |
| CN210021701U (en) * | 2019-03-08 | 2020-02-07 | 祝恩波 | Gas pollutant processor |
-
2019
- 2019-03-08 CN CN201910173851.9A patent/CN109731459A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE729053A (en) * | 1968-05-07 | 1969-08-01 | ||
| FR2473493A1 (en) * | 1979-09-28 | 1981-07-17 | Tomenko Viktor | Carbonisation column for sodium hydrogen carbonate prodn. - has perforated plates, overflows and cooling pipes arranged to increase heat and material exchange |
| CN205461674U (en) * | 2016-01-17 | 2016-08-17 | 刘伟华 | Exhaust gases filter tower |
| CN206543510U (en) * | 2017-01-18 | 2017-10-10 | 上海杓玉医药科技有限公司 | A kind of tail gas absorber of phenmethylol production |
| CN207928959U (en) * | 2018-01-19 | 2018-10-02 | 天津浩元精细化工股份有限公司 | A kind of circulated sprinkling tail gas absorber |
| CN108815992A (en) * | 2018-07-20 | 2018-11-16 | 祝恩波 | The air pollutants processor of heat-recoverable |
| CN108826760A (en) * | 2018-07-23 | 2018-11-16 | 麦克维尔空调制冷(武汉)有限公司 | The multistage flooded evaporator of spiracular plate structure and anti-absorbing gas belt liquid |
| CN210021701U (en) * | 2019-03-08 | 2020-02-07 | 祝恩波 | Gas pollutant processor |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110980596A (en) * | 2019-12-18 | 2020-04-10 | 王信荣 | Forklift internal combustion engine cover with cooling and odor removing functions |
| CN111495159A (en) * | 2020-05-29 | 2020-08-07 | 祝恩波 | Processor for automatically adjusting gas pollutant discharge value |
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| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20190510 |
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| RJ01 | Rejection of invention patent application after publication |