CN106178904A - A kind of emission-control equipment and waste gas processing method - Google Patents
A kind of emission-control equipment and waste gas processing method Download PDFInfo
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- CN106178904A CN106178904A CN201610812968.3A CN201610812968A CN106178904A CN 106178904 A CN106178904 A CN 106178904A CN 201610812968 A CN201610812968 A CN 201610812968A CN 106178904 A CN106178904 A CN 106178904A
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- Prior art keywords
- conservation tank
- reactor
- waste
- tank
- outlet
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- 239000002912 waste gases Substances 0.000 title claims abstract description 66
- 238000003672 processing method Methods 0.000 title claims abstract description 14
- 239000003638 reducing agents Substances 0.000 claims abstract description 42
- 238000006243 chemical reactions Methods 0.000 claims abstract description 38
- 239000007788 liquids Substances 0.000 claims description 83
- 239000011901 water Substances 0.000 claims description 80
- 239000002699 waste materials Substances 0.000 claims description 45
- 230000001105 regulatory Effects 0.000 claims description 24
- 239000003570 air Substances 0.000 claims description 22
- 239000007789 gases Substances 0.000 claims description 21
- 230000003068 static Effects 0.000 claims description 21
- 241001081830 Degeneriaceae Species 0.000 claims description 14
- UIIMBOGNXHQVGW-UHFFFAOYSA-M NaHCO3 Chemical compound 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NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 14
- 230000001276 controlling effects Effects 0.000 claims description 6
- -1 aqua calcis Substances 0.000 claims description 4
- 230000005540 biological transmission Effects 0.000 claims 1
- 238000000034 methods Methods 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 5
- 239000000126 substances Substances 0.000 abstract 1
- 230000003009 desulfurizing Effects 0.000 description 7
- 239000000292 calcium oxide Substances 0.000 description 6
- 229910000118 calcium oxide Inorganic materials 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 6
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- 229910052739 hydrogen Inorganic materials 0.000 description 6
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- 238000006477 desulfuration reactions Methods 0.000 description 2
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- 239000003513 alkali Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 238000002485 combustion reactions Methods 0.000 description 1
- 239000000686 essences Substances 0.000 description 1
- 239000000295 fuel oils Substances 0.000 description 1
- 238000002372 labelling Methods 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound 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[Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 229910052751 metals Inorganic materials 0.000 description 1
- 239000002184 metals Substances 0.000 description 1
- 239000000203 mixtures Substances 0.000 description 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitric oxide Chemical class 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O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 1
- 229910052813 nitrogen oxides Inorganic materials 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 229910052815 sulfur oxides Inorganic materials 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/60—Simultaneously removing sulfur oxides and nitrogen oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/20—Reductants
- B01D2251/206—Ammonium compounds
- B01D2251/2062—Ammonia
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/20—Reductants
- B01D2251/206—Ammonium compounds
- B01D2251/2067—Urea
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/30—Alkali metal compounds
- B01D2251/304—Alkali metal compounds of sodium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/40—Alkaline earth metal or magnesium compounds
- B01D2251/404—Alkaline earth metal or magnesium compounds of calcium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/60—Inorganic bases or salts
- B01D2251/604—Hydroxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/60—Inorganic bases or salts
- B01D2251/606—Carbonates
Abstract
Description
Technical field
The present invention relates to exhaust-gas treatment field, be specifically a kind of emission-control equipment and waste gas processing method.
Background technology
Along with China's industrial expansion, annual waste gas discharge capacity steeply rises, the serious ecological environment having influence on China Quality.When coal or heavy oil combustion produce waste gas in, comprise coal dust, oxysulfide, nitrogen oxides, etc..In recent years, have studied With the denitrification apparatus that NOx is reduced and utilize Alkali absorption liquid remove SOx wet desulfurizer process mercury metal in combination Device and method.
But there is desulfurizing agent in current desulfurization and method of denitration and denitrification reducing agent waste is serious and under-supply double Reappearing field, when desulfurizing agent and denitrification reducing agent deficiency when, the treatment effect of waste gas also can be substantially reduced, and is arranged by these waste gas The when of being put in the middle of air, certainly will seriously arrive atmospheric environment.
Summary of the invention
It is an object of the invention to: for the problem of above-mentioned existence, it is provided that one can control desulfurizing agent and denitrfying agent simultaneously Each concentration of component and the emission-control equipment of flow and waste gas processing method.
The technical solution used in the present invention is as follows:
The invention discloses a kind of emission-control equipment, provide device, waste gas including exhaust gas inlet pipe, reaction unit, reducing agent Outlet, described exhaust gas inlet pipe, reducing agent provide device, waste gas outlet pipe to be connected with reaction unit respectively.
As improvement, described reaction unit includes the first reactor, the second reactor, described the first reactor, Two reactors are equipped with air inlet and gas outlet, and the air inlet of the first reactor connects exhaust gas inlet pipeline, the first reactor Gas outlet connects the air inlet of the second reactor, and the gas outlet of the second reactor connects waste gas outlet pipe;
Described the first reactor, the bottom of the second reactor are provided with liquid outlet, and described liquid outlet is connected by pipeline To waste liquid outlet.
As improvement, described reducing agent provide device include the first conservation tank, the second conservation tank, the 3rd conservation tank, the Four conservation tanks, running water inlet pipe, static mixer, valve, water pump, described the first conservation tank, the second conservation tank, the 3rd storage Standby tank, the 4th conservation tank, running water inlet pipe are connected with static mixer respectively, and described static mixer and valve connect, Valve and water pump connect.
As improvement, described reducing agent provides the pipeline between device and reaction unit to be provided with temperature regulating device, described Temperature regulating device guarantee replacement central processing unit, the temperature sensor being connected with central processing unit and heater, described temperature passes Sensor is connected to upstream or the downstream of heater, and described temperature regulating device is set with certain temperature value T, and temperature sensor will The temperature signal of the liquid sensed is delivered to central processing unit, and when temperature signal is less than (T-5) DEG C when, central authorities process Heating signal is delivered to heater and heats by device, and when temperature signal is higher than (T+5) DEG C when, central processing unit will stop Only the signal of heating is delivered to heater.
As improvement, between described temperature regulating device and reaction unit, it is additionally provided with metering device, described metering device bag Including storage tank, water pump, dosing pump, described storage tank and water pump to connect, described water pump and dosing pump connect, described water pump It is provided with pipeline with the pipeline on dosing pump to be connected on storage tank.
As improvement, it is provided with control reducing agent, the control system of water supply, and described control system includes at control Reason device, set with the inlet exhaust detector on exhaust gas inlet pipe, be provided with on waste gas outlet pipe outlet exhaust detector, be provided with useless Liquid outlet on waste liquid outlet detector, be respectively equipped with the first conservation tank, the second conservation tank, the 3rd conservation tank, the 4th conservation tank, Volume control device on running water inlet pipe；
Described inlet exhaust detector, outlet exhaust detector, waste liquid outlet detector and the first conservation tank, the second deposit Volume control device on tank, the 3rd conservation tank, the 4th conservation tank, running water inlet pipe connects with control processor respectively；
Described inlet exhaust detector, outlet exhaust detector are equipped with and can identify that the waste gas of variety classes exhaust gas concentration is dense Degree sensor and waste gas flow sensor；
Described waste liquid outlet detector is provided with liquid waste concentration sensor and the waste liquid flow velocity identifying variety classes liquid waste concentration Sensor.
The present invention discloses a kind of waste gas processing method using emission-control equipment of the present invention, it is characterised in that Described the first conservation tank, the second conservation tank, the 3rd conservation tank, the 4th conservation tank are respectively equipped with urea liquid, ammonia spirit, hydrogen Calcium oxide solution, sodium bicarbonate solution, described urea liquid, ammonia spirit, aqua calcis, the weight of sodium bicarbonate solution Amount concentration is respectively 1%-20%, 1%-20%, 1%-5%, 1%-5%.
As improvement, the first described reactor, the inside of the second reactor is width alternating structure.
In sum, owing to have employed technique scheme, the beneficial effects of the present invention is:
1, emission-control equipment disclosed by the invention can be useless according to the flow velocity of inlet exhaust and the concentration of each component and outlet The flow velocity of gas and concentration select preferably reducing agent to provide the concentration of each component of device, are possible not only to improve the process effect of waste gas Really, and the minimum of cost can be reached；
2, reactor disclosed by the invention uses width to replace cross-section mechanism, participates in reaction time waste gas has sufficient wherein, Improve desulfurization and denitration effect；
3, the present invention can monitor the concentration of each component of waste liquid in real time, selects preferably also according to the concentration of each component of waste liquid simultaneously Former dose and desulfurizing agent concentration of component, reach the best results of reducing agent and desulfurizing agent.
Accompanying drawing explanation
Fig. 1 is the flow chart of emission-control equipment of the present invention；
Labelling in figure: 1-exhaust gas inlet pipe, 2-reaction unit, 21-the first reactor, 22-the second reactor, 23-waste liquid outlet, 3-reducing agent provides device, 31-the first conservation tank, 32-the second conservation tank, 33-the 3rd conservation tank, 34-the first conservation tank, 35- Running water inlet pipe, 36-static mixer, 37-valve, 38-water pump a, 4-temperature regulating device, 41-central processing unit, 42-heats Device, 5-storage tank, 6-water pump b, 7-dosing pump, 8-waste gas outlet pipe, 9-controls processor.
Detailed description of the invention
Below in conjunction with the accompanying drawings, the present invention is described in detail.
In order to make the purpose of the present invention, technical scheme and advantage clearer, below in conjunction with drawings and Examples, right The present invention is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the present invention, and It is not used in the restriction present invention.
Specific embodiment 1: as it is shown in figure 1, present embodiment discloses a kind of emission-control equipment, including exhaust gas inlet pipe 1, Reaction unit 2, reducing agent provide device 3, waste gas outlet pipe 8, described exhaust gas inlet pipe 1, reducing agent to provide device 3, waste gas Outlet 8 is connected with reaction unit 2 respectively.
Described reaction unit 2 includes first reactor the 21, second reactor 22, the first described reactor 21, second Reactor 22 is equipped with air inlet and gas outlet, and the air inlet of the first reactor connects exhaust gas inlet pipeline, the first reactor 21 Gas outlet connect the air inlet of the second reactor 22, the gas outlet of the second reactor connects waste gas outlet pipe 8;
The bottom of first described reactor the 21, second reactor 22 is provided with liquid outlet, and described liquid outlet passes through pipeline It is connected to waste liquid outlet (23).
Described reducing agent provides device 3 to include first conservation tank the 31, second conservation tank the 32, the 3rd conservation tank the 33, the 4th Conservation tank 34, running water inlet pipe 35, static mixer 36, valve 37, water pump a(38), the first described conservation tank 31, second Conservation tank the 32, the 3rd conservation tank the 33, the 4th conservation tank 34, running water inlet pipe 35 are connected with static mixer 36 respectively, described Static mixer 36 and valve 37 connect, valve 37 and water pump a38 connect.
Described reducing agent provides the pipeline between device 3 and reaction unit 2 to be provided with temperature regulating device 4, described temperature control Device is guaranteed replacement central processing unit 41, the temperature sensor being connected with central processing unit 41 and heater 42, and described temperature passes Sensor is connected to the upstream of heater, and described temperature regulating device 4 is set with certain temperature value T, and temperature sensor will be sensed To the temperature signal of liquid be delivered to central processing unit 41, when temperature signal less than (T-5) DEG C when, central processing unit will Heating signal is delivered to heater 42 and heats, and when temperature signal is higher than (T+5) DEG C when, central processing unit will stop The signal of heating is delivered to heater 42.
Being additionally provided with metering device between described temperature regulating device 4 and reaction unit 2, described metering device includes storage tank 5, water pump b6, dosing pump 7, described storage tank 5 and water pump b6 connect, and described water pump b6 and dosing pump 7 connect, described water Pipeline on pump b6 and dosing pump 7 is provided with pipeline and is connected on storage tank 5.
Emission-control equipment is provided with control reducing agent, the control system of water supply, and described control system includes controlling Processor 9, set with the inlet exhaust detector on exhaust gas inlet pipe 1, be provided with on waste gas outlet pipe 8 outlet exhaust detector, The waste liquid outlet detector that is provided with on waste liquid outlet 23, it is respectively equipped with first conservation tank the 31, second conservation tank the 32, the 3rd conservation tank 33, the volume control device on the 4th conservation tank 34, running water inlet pipe 35；
Described inlet exhaust detector, outlet exhaust detector, waste liquid outlet detector and the first conservation tank 31, second store up Volume control device on standby tank the 32, the 3rd conservation tank the 33, the 4th conservation tank 34, running water inlet pipe 35 processes with control respectively Device connects；
Described inlet exhaust detector, outlet exhaust detector are equipped with and can identify that the waste gas of variety classes exhaust gas concentration is dense Degree sensor and waste gas flow sensor；
Described waste liquid outlet detector is provided with liquid waste concentration sensor and the waste liquid flow velocity identifying variety classes liquid waste concentration Sensor.
The first described reactor 21, the inside of the second reactor 22 is width alternating structure.
The present embodiment also discloses a kind of waste gas processing method using emission-control equipment disclosed in the present embodiment, First conservation tank the 31, second conservation tank the 32, the 3rd conservation tank the 33, the 4th conservation tank is respectively equipped with urea liquid, ammonia spirit, hydrogen Calcium oxide solution, sodium bicarbonate solution, described urea liquid, ammonia spirit, aqua calcis, the weight of sodium bicarbonate solution Amount concentration is 1%.
Specific embodiment 2: present embodiment discloses a kind of emission-control equipment, including exhaust gas inlet pipe 1, reaction unit 2, Reducing agent provides device 3, waste gas outlet pipe 8, described exhaust gas inlet pipe 1, reducing agent to provide device 3, waste gas outlet pipe 8 respectively It is connected with reaction unit 2.
Described reaction unit 2 includes first reactor the 21, second reactor 22, the first described reactor 21, second Reactor 22 is equipped with air inlet and gas outlet, and the air inlet of the first reactor connects exhaust gas inlet pipeline, the first reactor 21 Gas outlet connect the air inlet of the second reactor 22, the gas outlet of the second reactor connects waste gas outlet pipe 8;
The bottom of first described reactor the 21, second reactor 22 is provided with liquid outlet, and described liquid outlet passes through pipeline It is connected to waste liquid outlet (23).
Described reducing agent provides device 3 to include first conservation tank the 31, second conservation tank the 32, the 3rd conservation tank the 33, the 4th Conservation tank 34, running water inlet pipe 35, static mixer 36, valve 37, water pump a(38), the first described conservation tank 31, second Conservation tank the 32, the 3rd conservation tank the 33, the 4th conservation tank 34, running water inlet pipe 35 are connected with static mixer 36 respectively, described Static mixer 36 and valve 37 connect, valve 37 and water pump a38 connect.
Described reducing agent provides the pipeline between device 3 and reaction unit 2 to be provided with temperature regulating device 4, described temperature control Device is guaranteed replacement central processing unit 41, the temperature sensor being connected with central processing unit 41 and heater 42, and described temperature passes Sensor is connected to the downstream of heater, and described temperature regulating device 4 is set with certain temperature value T, and temperature sensor will be sensed To the temperature signal of liquid be delivered to central processing unit 41, when temperature signal less than (T-5) DEG C when, central processing unit will Heating signal is delivered to heater 42 and heats, and when temperature signal is higher than (T+5) DEG C when, central processing unit will stop The signal of heating is delivered to heater 42.
Being additionally provided with metering device between described temperature regulating device 4 and reaction unit 2, described metering device includes storage tank 5, water pump b6, dosing pump 7, described storage tank 5 and water pump b6 connect, and described water pump b6 and dosing pump 7 connect, described water Pipeline on pump b6 and dosing pump 7 is provided with pipeline and is connected on storage tank 5.
Emission-control equipment is provided with control reducing agent, the control system of water supply, and described control system includes controlling Processor 9, set with the inlet exhaust detector on exhaust gas inlet pipe 1, be provided with on waste gas outlet pipe 8 outlet exhaust detector, The waste liquid outlet detector that is provided with on waste liquid outlet 23, it is respectively equipped with first conservation tank the 31, second conservation tank the 32, the 3rd conservation tank 33, the volume control device on the 4th conservation tank 34, running water inlet pipe 35；
Described inlet exhaust detector, outlet exhaust detector, waste liquid outlet detector and the first conservation tank 31, second store up Volume control device on standby tank the 32, the 3rd conservation tank the 33, the 4th conservation tank 34, running water inlet pipe 35 processes with control respectively Device connects；
Described inlet exhaust detector, outlet exhaust detector are equipped with and can identify that the waste gas of variety classes exhaust gas concentration is dense Degree sensor and waste gas flow sensor；
Described waste liquid outlet detector is provided with liquid waste concentration sensor and the waste liquid flow velocity identifying variety classes liquid waste concentration Sensor.
The first described reactor 21, the inside of the second reactor 22 is width alternating structure.
The present embodiment also discloses a kind of waste gas processing method using emission-control equipment disclosed in the present embodiment, First conservation tank the 31, second conservation tank the 32, the 3rd conservation tank the 33, the 4th conservation tank is respectively equipped with urea liquid, ammonia spirit, hydrogen Calcium oxide solution, sodium bicarbonate solution, described urea liquid, ammonia spirit, aqua calcis, the weight of sodium bicarbonate solution Amount concentration is respectively 20%, 20%, 5%, 5%.
Specific embodiment 3: as it is shown in figure 1, present embodiment discloses a kind of emission-control equipment, including exhaust gas inlet pipe 1, Reaction unit 2, reducing agent provide device 3, waste gas outlet pipe 8, described exhaust gas inlet pipe 1, reducing agent to provide device 3, waste gas Outlet 8 is connected with reaction unit 2 respectively.
Described reaction unit 2 includes first reactor the 21, second reactor 22, the first described reactor 21, second Reactor 22 is equipped with air inlet and gas outlet, and the air inlet of the first reactor connects exhaust gas inlet pipeline, the first reactor 21 Gas outlet connect the air inlet of the second reactor 22, the gas outlet of the second reactor connects waste gas outlet pipe 8;
The bottom of first described reactor the 21, second reactor 22 is provided with liquid outlet, and described liquid outlet passes through pipeline It is connected to waste liquid outlet (23).
Described reducing agent provides device 3 to include first conservation tank the 31, second conservation tank the 32, the 3rd conservation tank the 33, the 4th Conservation tank 34, running water inlet pipe 35, static mixer 36, valve 37, water pump a(38), the first described conservation tank 31, second Conservation tank the 32, the 3rd conservation tank the 33, the 4th conservation tank 34, running water inlet pipe 35 are connected with static mixer 36 respectively, described Static mixer 36 and valve 37 connect, valve 37 and water pump a38 connect.
Described reducing agent provides the pipeline between device 3 and reaction unit 2 to be provided with temperature regulating device 4, described temperature control Device is guaranteed replacement central processing unit 41, the temperature sensor being connected with central processing unit 41 and heater 42, and described temperature passes Sensor is connected to the upstream of heater, and described temperature regulating device 4 is set with certain temperature value T, and temperature sensor will be sensed To the temperature signal of liquid be delivered to central processing unit 41, when temperature signal less than (T-5) DEG C when, central processing unit will Heating signal is delivered to heater 42 and heats, and when temperature signal is higher than (T+5) DEG C when, central processing unit will stop The signal of heating is delivered to heater 42.
Being additionally provided with metering device between described temperature regulating device 4 and reaction unit 2, described metering device includes storage tank 5, water pump b6, dosing pump 7, described storage tank 5 and water pump b6 connect, and described water pump b6 and dosing pump 7 connect, described water Pipeline on pump b6 and dosing pump 7 is provided with pipeline and is connected on storage tank 5.
Emission-control equipment is provided with control reducing agent, the control system of water supply, and described control system includes controlling Processor 9, set with the inlet exhaust detector on exhaust gas inlet pipe 1, be provided with on waste gas outlet pipe 8 outlet exhaust detector, The waste liquid outlet detector that is provided with on waste liquid outlet 23, it is respectively equipped with first conservation tank the 31, second conservation tank the 32, the 3rd conservation tank 33, the volume control device on the 4th conservation tank 34, running water inlet pipe 35；
Described inlet exhaust detector, outlet exhaust detector, waste liquid outlet detector and the first conservation tank 31, second store up Volume control device on standby tank the 32, the 3rd conservation tank the 33, the 4th conservation tank 34, running water inlet pipe 35 processes with control respectively Device connects；
Described inlet exhaust detector, outlet exhaust detector are equipped with and can identify that the waste gas of variety classes exhaust gas concentration is dense Degree sensor and waste gas flow sensor；
Described waste liquid outlet detector is provided with liquid waste concentration sensor and the waste liquid flow velocity identifying variety classes liquid waste concentration Sensor.
The first described reactor 21, the inside of the second reactor 22 is width alternating structure.
The present embodiment also discloses a kind of waste gas processing method using emission-control equipment disclosed in the present embodiment, First conservation tank the 31, second conservation tank the 32, the 3rd conservation tank the 33, the 4th conservation tank is respectively equipped with urea liquid, ammonia spirit, hydrogen Calcium oxide solution, sodium bicarbonate solution, described urea liquid, ammonia spirit, aqua calcis, the weight of sodium bicarbonate solution Amount concentration is respectively 10%, 7%, 2%, 3%.
Specific embodiment 4: as it is shown in figure 1, present embodiment discloses a kind of emission-control equipment, including exhaust gas inlet pipe 1, Reaction unit 2, reducing agent provide device 3, waste gas outlet pipe 8, described exhaust gas inlet pipe 1, reducing agent to provide device 3, waste gas Outlet 8 is connected with reaction unit 2 respectively.
Described reaction unit 2 includes first reactor the 21, second reactor 22, the first described reactor 21, second Reactor 22 is equipped with air inlet and gas outlet, and the air inlet of the first reactor connects exhaust gas inlet pipeline, the first reactor 21 Gas outlet connect the air inlet of the second reactor 22, the gas outlet of the second reactor connects waste gas outlet pipe 8;
The bottom of first described reactor the 21, second reactor 22 is provided with liquid outlet, and described liquid outlet passes through pipeline It is connected to waste liquid outlet (23).
Described reducing agent provides device 3 to include first conservation tank the 31, second conservation tank the 32, the 3rd conservation tank the 33, the 4th Conservation tank 34, running water inlet pipe 35, static mixer 36, valve 37, water pump a(38), the first described conservation tank 31, second Conservation tank the 32, the 3rd conservation tank the 33, the 4th conservation tank 34, running water inlet pipe 35 are connected with static mixer 36 respectively, described Static mixer 36 and valve 37 connect, valve 37 and water pump a38 connect.
Described reducing agent provides the pipeline between device 3 and reaction unit 2 to be provided with temperature regulating device 4, described temperature control Device is guaranteed replacement central processing unit 41, the temperature sensor being connected with central processing unit 41 and heater 42, and described temperature passes Sensor is connected to the upstream of heater, and described temperature regulating device 4 is set with certain temperature value T, and temperature sensor will be sensed To the temperature signal of liquid be delivered to central processing unit 41, when temperature signal less than (T-5) DEG C when, central processing unit will Heating signal is delivered to heater 42 and heats, and when temperature signal is higher than (T+5) DEG C when, central processing unit will stop The signal of heating is delivered to heater 42.
Being additionally provided with metering device between described temperature regulating device 4 and reaction unit 2, described metering device includes storage tank 5, water pump b6, dosing pump 7, described storage tank 5 and water pump b6 connect, and described water pump b6 and dosing pump 7 connect, described water Pipeline on pump b6 and dosing pump 7 is provided with pipeline and is connected on storage tank 5.
Emission-control equipment is provided with control reducing agent, the control system of water supply, and described control system includes controlling Processor 9, set with the inlet exhaust detector on exhaust gas inlet pipe 1, be provided with on waste gas outlet pipe 8 outlet exhaust detector, The waste liquid outlet detector that is provided with on waste liquid outlet 23, it is respectively equipped with first conservation tank the 31, second conservation tank the 32, the 3rd conservation tank 33, the volume control device on the 4th conservation tank 34, running water inlet pipe 35；
Described inlet exhaust detector, outlet exhaust detector, waste liquid outlet detector and the first conservation tank 31, second store up Volume control device on standby tank the 32, the 3rd conservation tank the 33, the 4th conservation tank 34, running water inlet pipe 35 processes with control respectively Device connects；
Described inlet exhaust detector, outlet exhaust detector are equipped with and can identify that the waste gas of variety classes exhaust gas concentration is dense Degree sensor and waste gas flow sensor；
Described waste liquid outlet detector is provided with liquid waste concentration sensor and the waste liquid flow velocity identifying variety classes liquid waste concentration Sensor.
The first described reactor 21, the inside of the second reactor 22 is width alternating structure.
The present embodiment also discloses a kind of waste gas processing method using emission-control equipment disclosed in the present embodiment, First conservation tank the 31, second conservation tank the 32, the 3rd conservation tank the 33, the 4th conservation tank is respectively equipped with urea liquid, ammonia spirit, hydrogen Calcium oxide solution, sodium bicarbonate solution, described urea liquid, ammonia spirit, aqua calcis, the weight of sodium bicarbonate solution Amount concentration is respectively 1%, 1%, 5%, 5%.
Specific embodiment 5: as it is shown in figure 1, present embodiment discloses a kind of emission-control equipment, including exhaust gas inlet pipe 1, Reaction unit 2, reducing agent provide device 3, waste gas outlet pipe 8, described exhaust gas inlet pipe 1, reducing agent to provide device 3, waste gas Outlet 8 is connected with reaction unit 2 respectively.
Described reaction unit 2 includes first reactor the 21, second reactor 22, the first described reactor 21, second Reactor 22 is equipped with air inlet and gas outlet, and the air inlet of the first reactor connects exhaust gas inlet pipeline, the first reactor 21 Gas outlet connect the air inlet of the second reactor 22, the gas outlet of the second reactor connects waste gas outlet pipe 8;
The bottom of first described reactor the 21, second reactor 22 is provided with liquid outlet, and described liquid outlet passes through pipeline It is connected to waste liquid outlet (23).
Described reducing agent provides device 3 to include first conservation tank the 31, second conservation tank the 32, the 3rd conservation tank the 33, the 4th Conservation tank 34, running water inlet pipe 35, static mixer 36, valve 37, water pump a(38), the first described conservation tank 31, second Conservation tank the 32, the 3rd conservation tank the 33, the 4th conservation tank 34, running water inlet pipe 35 are connected with static mixer 36 respectively, described Static mixer 36 and valve 37 connect, valve 37 and water pump a38 connect.
Described reducing agent provides the pipeline between device 3 and reaction unit 2 to be provided with temperature regulating device 4, described temperature control Device is guaranteed replacement central processing unit 41, the temperature sensor being connected with central processing unit 41 and heater 42, and described temperature passes Sensor is connected to the upstream of heater, and described temperature regulating device 4 is set with certain temperature value T, and temperature sensor will be sensed To the temperature signal of liquid be delivered to central processing unit 41, when temperature signal less than (T-5) DEG C when, central processing unit will Heating signal is delivered to heater 42 and heats, and when temperature signal is higher than (T+5) DEG C when, central processing unit will stop The signal of heating is delivered to heater 42.
Being additionally provided with metering device between described temperature regulating device 4 and reaction unit 2, described metering device includes storage tank 5, water pump b6, dosing pump 7, described storage tank 5 and water pump b6 connect, and described water pump b6 and dosing pump 7 connect, described water Pipeline on pump b6 and dosing pump 7 is provided with pipeline and is connected on storage tank 5.
Emission-control equipment is provided with control reducing agent, the control system of water supply, and described control system includes controlling Processor 9, set with the inlet exhaust detector on exhaust gas inlet pipe 1, be provided with on waste gas outlet pipe 8 outlet exhaust detector, The waste liquid outlet detector that is provided with on waste liquid outlet 23, it is respectively equipped with first conservation tank the 31, second conservation tank the 32, the 3rd conservation tank 33, the volume control device on the 4th conservation tank 34, running water inlet pipe 35；
Described inlet exhaust detector, outlet exhaust detector, waste liquid outlet detector and the first conservation tank 31, second store up Volume control device on standby tank the 32, the 3rd conservation tank the 33, the 4th conservation tank 34, running water inlet pipe 35 processes with control respectively Device connects；
Described inlet exhaust detector, outlet exhaust detector are equipped with and can identify that the waste gas of variety classes exhaust gas concentration is dense Degree sensor and waste gas flow sensor；
Described waste liquid outlet detector is provided with liquid waste concentration sensor and the waste liquid flow velocity identifying variety classes liquid waste concentration Sensor.
The first described reactor 21, the inside of the second reactor 22 is width alternating structure.
The present embodiment also discloses a kind of waste gas processing method using emission-control equipment disclosed in the present embodiment, First conservation tank the 31, second conservation tank the 32, the 3rd conservation tank the 33, the 4th conservation tank is respectively equipped with urea liquid, ammonia spirit, hydrogen Calcium oxide solution, sodium bicarbonate solution, described urea liquid, ammonia spirit, aqua calcis, the weight of sodium bicarbonate solution Amount concentration is respectively 20%, 20%, 1%, 1%.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all essences in the present invention Any amendment, equivalent and the improvement etc. made within god and principle, should be included within the scope of the present invention.
Claims (8)
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Application publication date: 20161207 |