CN116857657A - Garbage incinerator and purification process thereof - Google Patents
Garbage incinerator and purification process thereof Download PDFInfo
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- CN116857657A CN116857657A CN202211400536.3A CN202211400536A CN116857657A CN 116857657 A CN116857657 A CN 116857657A CN 202211400536 A CN202211400536 A CN 202211400536A CN 116857657 A CN116857657 A CN 116857657A
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- flue gas
- gas
- frequency
- removal
- inlet
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- 238000000746 purification Methods 0.000 title claims description 12
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000003546 flue gas Substances 0.000 claims abstract description 34
- 238000004140 cleaning Methods 0.000 claims abstract description 16
- 238000000034 method Methods 0.000 claims abstract description 11
- 239000007789 gas Substances 0.000 claims description 50
- 239000003344 environmental pollutant Substances 0.000 claims description 38
- 231100000719 pollutant Toxicity 0.000 claims description 34
- 230000008878 coupling Effects 0.000 claims description 24
- 238000010168 coupling process Methods 0.000 claims description 24
- 238000005859 coupling reaction Methods 0.000 claims description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 21
- 239000000428 dust Substances 0.000 claims description 17
- 238000005507 spraying Methods 0.000 claims description 16
- 239000007788 liquid Substances 0.000 claims description 13
- 238000001914 filtration Methods 0.000 claims description 11
- 239000002245 particle Substances 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 230000008569 process Effects 0.000 claims description 10
- 230000007423 decrease Effects 0.000 claims description 8
- 238000001514 detection method Methods 0.000 claims description 6
- 239000000356 contaminant Substances 0.000 claims description 5
- 238000013461 design Methods 0.000 claims description 5
- 238000004064 recycling Methods 0.000 claims description 3
- 239000000779 smoke Substances 0.000 abstract description 6
- 238000012423 maintenance Methods 0.000 abstract 1
- 239000002699 waste material Substances 0.000 abstract 1
- 208000028659 discharge Diseases 0.000 description 13
- 230000000694 effects Effects 0.000 description 10
- 238000005265 energy consumption Methods 0.000 description 8
- 238000005457 optimization Methods 0.000 description 6
- 239000007921 spray Substances 0.000 description 6
- 239000003595 mist Substances 0.000 description 5
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 238000004056 waste incineration Methods 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 230000006378 damage Effects 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 230000036541 health Effects 0.000 description 3
- 238000004088 simulation Methods 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000003916 acid precipitation Methods 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000002341 toxic gas Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000009739 binding Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000010891 toxic waste Substances 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
- F23J15/025—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using filters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Treating Waste Gases (AREA)
Abstract
The application relates to a boiler waste incinerator, which is provided with a shell with a smoke inlet and a smoke outlet; means for moving flue gas through the housing; means for directing the flue gas through the lower filter; an upper filter supported inside the housing at a position generally higher than the lower filter; means for directing the flue gas through the upper filter; each of the upper and lower filters includes a perforated sheet member positioned generally transverse to the flow of flue gas directed therethrough. An object of the present application is to provide an economical and practical apparatus and method for improving the operation state of a flue gas cleaning system of a garbage incinerator, increasing the treatment efficiency of the flue gas of the system, and reducing the maintenance cost.
Description
Technical Field
The application relates to a boiler system, in particular to a gas purifying device and a process for removing dust/fog and other multi-pollutant power plant boilers.
Background
A large amount of non-organized pollutants are often generated in the production process of boilers and the like. Toxic gases such as smoke dust, sulfur dioxide and the like can be generated after the combustion in the boiler. These are important factors that cause weather disasters such as haze and acid rain. Thereby causing environmental damage and economic loss and also causing harm to human health. In addition, waste incineration plants are often located near populated areas. The emission of boiler fumes also causes serious damage to the health of residents in the vicinity of the waste incineration power plant, and is therefore highly suspected by the residents. Therefore, it is important to make contribution to reducing weather disasters such as haze and acid rain and improving the quality of living environment of residents by improving a treatment system of waste incineration boiler flue gas and reducing toxic gases such as smoke dust, sulfur dioxide and the like discharged by the boiler flue gas to European Union standards. The circulating feeder adopted in the multi-component toxic waste gas treatment technology is easy to be blocked by a medium, so that a waste incineration boiler flue gas purification system is in fault. The main cause of the blockage is that the internal medium in the feeder is wetted, loosened and bound, so that the gap between the blade and the casing is easily blocked. If the problems of wetting, dissolution and binding are solved by the medium, the clogging situation can be improved.
Taking the rolling production process in the steel industry as an example, various pollutants, namely, fallen ferric oxide powder, cooling water vapor and lubricating oil mist, can be produced in the production, and the particles with the particle size of about 3-20 mu m can float in a workshop for a long time, so that a large amount of harmful smoke dust is formed. The main components of the flue gas are FeO and Fe 2 O 3 、H 2 O, oil mist, etc. In addition, in the high-temperature rolling process, the air on the surface of the steel is heated and rises, and moves together with dust; meanwhile, the water vapor generated in the cooling process is also outwards diffused under the action of still flow, so that smoke dust is emitted to the whole workshop, not only is strong visual pollution brought, but also heat exchange of production equipment and electric elements of corrosion equipment are influenced due to deposition blockage, and meanwhile, the physical health of operators is also influenced to a certain extent.
At present, the technology of centralized treatment after collection is mainly adopted for removing multi-pollutants generated in the production process, but the actual operation is affected by unreasonable design and arrangement of a collection cover, and the defects of low collection precision, extensive treatment, high operation energy consumption and the like are commonly existed, so that the treatment effect on the multi-pollutants generated in the production process is seriously affected.
Disclosure of Invention
In order to solve the problems, the application provides a gas purifying device for efficiently removing multiple pollutants such as dust/fog and the like, which comprises a multifunctional efficient collecting cover, a multi-force coupling removing tower, an intelligent control system and the like. The gas pollutants generated in the production process are efficiently collected and pretreated through the multifunctional efficient gas collecting hood, then enter the multi-force coupling removal tower to complete efficient removal, and the purified gas is led out by the induced draft fan.
In order to achieve the above purpose, the application adopts the following technical scheme:
a garbage incinerator having a housing with a flue gas inlet and a flue gas outlet; means for moving flue gas through the housing; means for directing the flue gas through the lower filter; an upper filter supported inside the housing at a position generally higher than the lower filter; means for directing the flue gas through the upper filter; each of the upper and lower filters includes a perforated sheet member positioned generally transverse to the flow of flue gas directed therethrough.
The means for directing the flue gas through the lower filter is a lower baffle, the lower filter comprising a first lower filter member connected to one of the edge flanges and a second lower filter member connected to the other of the edge flanges.
The lower baffle has a pair of transverse end walls, each of which is attached to the inlet duct.
A gas purification process for removing pollutants comprises a multifunctional efficient collecting cover and a multi-force coupling removing tower, wherein a sensor is arranged at an inlet at the bottom of the collecting cover, the sensor detects pollutants generated in the production process and transmits detection signals to an intelligent control system, the intelligent control system starts a #2 variable-frequency circulating pump, a #1 high-voltage power supply and a #2 high-voltage power supply according to the signals, and a variable-frequency induced draft fan, and meanwhile, the frequency of the circulating pump and/or the induced draft fan is adjusted according to the intensity of the detection signals;
the gas containing pollutants is uniformly sucked into a multifunctional collecting cover, particles such as dust/fog in the gas collide with charges generated by a charging device in a flue to be charged, collide with atomized liquid drops generated by a pretreatment nozzle to be agglomerated, grow and partially remove the dust/fog particles, water generated in the process is collected by the liquid drop collecting device and then is sent back to a circulating filtering water tank to be filtered, and then is sent back to the pretreatment nozzle for recycling through a #2 variable-frequency circulating pump;
and a flow sensor is arranged at the inlet at the bottom of the collecting cover, and the frequency of the fan is controlled according to the flow sensor.
When the detected flow rises, the power of the variable frequency induced draft fan is controlled to be increased, and when the detected flow drops, the power of the variable frequency induced draft fan is controlled to be reduced.
The device comprises a multifunctional efficient collecting cover and a multi-force coupling removing tower, wherein the removing tower is connected with the collecting cover through a pipeline, an air inlet groove is formed in the lower part of the collecting cover, an outlet pipeline is arranged on the upper part of the collecting cover, a charging device, a spraying device and a liquid drop collecting device are arranged in the outlet pipeline, the charging device is arranged in a cavity on the wall of the outlet pipeline, the spraying device is arranged on the upper part of the charging device, the collecting device is arranged on the lower part of the spraying device, and flue gas pretreated by charging and spraying enters the multi-force coupling removing tower; the device is characterized in that a cleaning nozzle and a multi-force coupling pollutant removal device are arranged in the removal tower, the cleaning nozzle is positioned at the upper part of the removal tower, the multi-force coupling pollutant removal device is positioned at the lower part of the cleaning nozzle, and the device comprises a plurality of baffle plates which are arranged at intervals and discharge electrodes arranged between adjacent baffle plates.
The lower part of the collecting cover is provided with a plurality of air inlet grooves, the widths of the air inlet grooves are different, and the widths of the air inlet grooves gradually increase along the direction from the center of the air inlet grooves to the edge.
In practical application, the frequency control satisfies the following relation:
the maximum design speed of the inlet airflow at the bottom of the collecting cover is V, and the maximum frequency of the corresponding pump and fan is 50Hz, so that when the inlet airflow speed is V, the frequencies of the circulating pump and the fan are:
a× (V/V) ×50, where the coefficient a satisfies: a is more than or equal to 1 and less than or equal to 1.2.
Compared with the prior art, the application has the following advantages:
1. the power of the pump is controlled according to the detected flow, the frequency of the automatic collocation fan can be increased or reduced according to the gas flow, so that the gas storage is controlled in a proper range, overhigh or overlow is avoided, the energy consumption of the system operation is reduced while the pollutants are efficiently treated, and the optimization of the system is achieved.
2. The collecting cover has the charge and spray pretreatment function, and can realize the efficient removal of pollutants such as dust/fog by combining the rear-end multi-force coupling removal tower;
3. the collecting cover is designed by adopting the constant pressure principle, so that the constant-speed collection of the gas in the whole collecting area can be realized, the collecting precision is improved, and the running cost is reduced;
4. the device designed by the application is provided with an intelligent control system, can intelligently operate according to the emission of pollutants, and further reduces the operation cost.
Drawings
FIG. 1 is a schematic view of a gas cleaning device for dust/mist and other multi-pollutants according to the present application;
FIG. 2 is a schematic view of the collection hood inlet slot width arrangement of the present application;
fig. 3 is a control flow diagram of the present application.
The names corresponding to the serial numbers in the figures are as follows:
1. an intelligent control system; 2. a multifunctional collection cover; 3. a temperature/humidity and pressure sensor; 4. a flue; 5. a droplet collection device; 6. a spraying device; 7. a charging device; 8. a multi-force coupling removal tower; 9. cleaning the nozzle; 10. a pollutant removing device is coupled with the plurality of forces; 11. #1 high voltage power supply; 12. variable frequency induced draft fan; 13. a circulating filtration water tank; 14. #1 a circulation pump; 15. #2 variable frequency circulation pump; 16. #2 high voltage power supply.
Detailed Description
The following will make additional description on the technical solution in the embodiment of the present application with reference to the drawings in the embodiment of the present application.
A garbage incinerator having a housing with a flue gas inlet and a flue gas outlet; means for moving flue gas through the housing; means for directing the flue gas through the lower filter; an upper filter supported inside the housing at a position generally higher than the lower filter; means for directing the flue gas through the upper filter; each of the upper and lower filters includes a perforated sheet member positioned generally transverse to the flow of flue gas directed therethrough.
The means for directing the flue gas through the lower filter is a lower baffle, the lower filter comprising a first lower filter member connected to one of the edge flanges and a second lower filter member connected to the other of the edge flanges.
The lower baffle has a pair of transverse end walls, each of which is attached to the inlet duct.
The gas purifying device comprises a multifunctional efficient collecting cover 2 and a multi-force coupling removing tower 8, wherein the removing tower 8 is connected with the collecting cover 2 through a pipeline, an air inlet groove is formed in the lower part of the collecting cover 2, an outlet pipeline is formed in the upper part of the collecting cover 2, a charging device 7, a spraying device 6 and a liquid drop collecting device 5 are arranged in the outlet pipeline, the charging device 7 is arranged in a cavity on the wall of the outlet pipeline, the spraying device 6 is arranged on the upper part of the charging device 7, the collecting device 5 is arranged on the lower part of the spraying device 6, and flue gas subjected to charging and spraying pretreatment enters the multi-force coupling removing tower 8; the cleaning nozzle 9 and the multi-force coupling pollutant removal device 10 are arranged in the removal tower, the cleaning nozzle 9 is positioned at the upper part of the removal tower, and the multi-force coupling pollutant removal device 10 is positioned at the lower part of the cleaning nozzle 9 and comprises a plurality of baffle plates which are arranged at intervals and discharge electrodes arranged between adjacent baffle plates.
Preferably, the voltage of the discharge electrode is greater than the voltage of the charging device 7.
The collecting cover has the functions of charge and spray pretreatment, gas is subjected to charge and spray pretreatment through the collecting cover, fine water mist is combined with low-power charge to carry out pretreatment, and the pretreated gas enters the removal tower to be treated through the high-power discharge electrode, so that the high-efficiency removal of pollutants such as dust/mist in the gas can be realized. The reasonable collocation of the two-stage treatment steps avoids the influence of particles on the purification effect, so that the purification effect is optimal. In contrast, it was found through extensive experimentation that the effect of contaminant removal is markedly poor if the sequence of several stages is not arranged according to the application. The sequential collocation of the several stages of the present application is therefore an inventive aspect of the present application.
The application sets the charge and spray pretreatment function device in the collecting cover, which simplifies the structure and reduces the cost while meeting the purification effect.
Preferably, a plurality of air intake grooves having different widths are provided in the lower portion of the collecting hood 2, and the widths of the air intake grooves gradually increase in the direction from the center of the air intake groove toward the side. According to the application, through the arrangement of the width of the air inlet groove, the collecting cover is designed by adopting the equal pressure principle, so that the constant-speed collection of the air in the whole collecting area can be realized, the collecting precision is improved, and the running cost is reduced.
Preferably, the width of the air intake groove gradually increases more and more along the center of the air intake groove toward the side. The design of the variation amplitude is also a structure optimized through a large number of experiments and numerical simulation, so that the constant-speed collection technical effect can be further realized, and the requirements of the application are more met.
The width of the air inlet groove is changed according to the following rule:
the total length of the air inlet groove is 2L, and the width of the outermost position is W Outer part The W law from the center position by the distance l is as follows: w=b×w Outer part +c*W Outer part *（l/L） a Wherein a, b, c are coefficients, satisfying the following requirements:
1.085<a<1.103，0.992<b+c<1.010，0.496<b<0.627。
as L/L increases, a gradually increases.
0.094<a<1.101，b+c=1，0.563<b<0.575。
The optimized formula is obtained through a large number of experiments and numerical simulation, so that the gas can reach optimized distribution, the constant-speed collection technical effect can be optimally realized, and the requirements of the application are more met.
Preferably, a circulating filter water tank 13 is included, and the circulating filter 13 is arranged at the lower part of the collecting cover and the removing tower 8. The liquid drop collecting device 5 is connected with the circulating filtering water tank 13, and the collected liquid drops flow into the circulating filtering water tank through a pipeline.
Preferably, the cleaning nozzles spray water and the collected liquid, are sent from the bottom of the removal tower to a circulating filtration water tank for filtration treatment, and then reintroduced into the nozzles via a #1 circulating pump 14.
Preferably, the charging device 7 and the discharge electrode are powered by a high voltage power supply.
Preferably, the discharge electrode includes a baffle plate disposed between the baffles.
Preferably, the gas inlet of the removal tower 8 is arranged at the upper part of the removal tower 8, the gas outlet is arranged at the lower part of the removal tower 8, and the gas outlet is provided with a variable frequency induced draft fan 12 for sucking the purified gas away. The cleaning nozzle is provided at the upper part of the removal tower 8 and at the upper part of the gas inlet. Through setting up cleaning nozzle and gas inlet in upper portion for gas and spray liquid one direction motion, along the downward direction contact discharge electrode simultaneously when mixing with water, can improve purifying effect.
Preferably, the voltage of the discharge electrode is gradually increased along the flow direction of the gas in the stripping column 8 (e.g., the top-down direction of fig. 1). Because the amount of pollutants in the gas gradually decreases along with the flow of the gas, the voltage gradually increases through the discharge stage, so that the decontamination capability in the whole gas flow direction is basically the same, the countercurrent heat exchange effect similar to that of a heat exchanger is formed, and the purification capability is integrally improved through the distribution of the voltage under the condition that the overall voltage is unchanged.
It is further preferred that the voltage of the discharge electrode gradually increases in magnitude along the flow direction of the gas in the stripping column 8 (e.g., the top-down direction of fig. 1). The voltage amplitude variation is also a structure optimized through a large number of experiments and numerical simulation, the constant-speed collection technical effect can be further realized, and under the condition that the overall voltage is unchanged, the purification capability can be further integrally improved through the distribution of the voltage.
Preferably, a temperature, humidity and/or pressure sensor can be installed at the inlet at the bottom of the collecting cover according to the requirement, and the frequency of the switch and the fan frequency converter of the high-voltage power supply, the circulating pump and the fan can be controlled according to the detected temperature, humidity and speed change. Taking a pressure sensor as an example, it tests the change in the velocity of the inlet air flow at the bottom of the collection hood by measuring the change in the pressure differential. When the increase of the inlet airflow speed is detected, starting the #2 variable frequency circulating pump 15, the #1 high-voltage power supply 11 and the #2 high-voltage power supply 16 and the variable frequency induced draft fan 12 through the intelligent control system 1; as the inlet airflow speed continues to increase, the intelligent control system 1 will intelligently increase the frequency of the #2 variable frequency circulation pump 15 and the variable frequency induced draft fan 12. Through intelligent control, the system can efficiently treat pollutants and simultaneously reduce the energy consumption for system operation. In practical application, the frequency control satisfies the following relation:
the maximum design speed of the inlet airflow at the bottom of the collecting cover is V, and the maximum frequency of the corresponding pump and fan is 50Hz, so that when the inlet airflow speed is V, the frequencies of the circulating pump and the fan are:
a× (V/V) ×50, where the coefficient a satisfies: a is more than or equal to 1 and less than or equal to 1.2, and the value of a gradually becomes smaller as v increases; the maximum frequency does not exceed 50Hz.
Through the intelligent control, the system operation energy consumption can be reduced while the pollutants are efficiently treated, so that the optimization of the system is achieved.
Preferably, a temperature sensor is installed at the inlet of the bottom of the collecting hood, and the frequency of the circulation pumps 14, 15 is controlled based on the detected temperature.
When the detected temperature rises, the power of the circulation pumps 14, 15 is controlled to increase, and when the detected temperature falls, the power of the circulation pumps 14, 15 is controlled to fall. The power of the pump is controlled according to the detected temperature, so that the quantity of circulating water can be increased or reduced according to the gas temperature, the gas temperature is controlled in a proper range, the excessive high temperature or the excessive low temperature is avoided, the energy consumption of the system operation is reduced while the pollutants are efficiently treated, and the optimization of the system is achieved.
The inlet at the bottom of the collecting hood is provided with a humidity sensor, and the frequency of the circulating pumps 14 and 15 is controlled according to the detected humidity.
When the detected humidity decreases, the power of the circulation pumps 14, 15 is controlled to increase, and when the detected humidity decreases, the power of the circulation pumps 14, 15 is controlled to decrease. The power of the pump is controlled according to the detected humidity, so that the quantity of circulating water can be increased or reduced according to the gas humidity, the gas humidity is controlled in a proper range, the excessive high humidity or the excessive low humidity is avoided, the pump is matched with charge voltage, the pollutant is efficiently treated, the running energy consumption of a system is reduced, and the optimization of the system is achieved.
Flow sensors can be installed at the inlets at the bottom of the collecting hood as required, and the frequencies of the circulating pumps 14 and 15 can be controlled according to the flow sensors.
When the detected flow rate increases, the power of the circulation pumps 14, 15 is controlled to increase, and when the detected flow rate decreases, the power of the circulation pumps 14, 15 is controlled to decrease. The power of the pump is controlled according to the detected flow, so that the quantity of circulating water can be increased or reduced according to the gas flow, the gas storage is controlled in a proper range, and excessive high or excessive low is avoided, so that the energy consumption of the system operation is reduced while the pollutants are efficiently treated, and the optimization of the system is achieved.
A flow sensor can be arranged at the inlet at the bottom of the collecting cover according to the requirement, and the frequency of the variable-frequency induced draft fan 12 is controlled according to the flow sensor.
When the detected flow rises, the power of the variable frequency induced draft fan is controlled to be increased, and when the detected flow drops, the power of the variable frequency induced draft fan is controlled to be reduced. The power of the pump is controlled according to the detected flow, the frequency of the automatic collocation fan can be increased or reduced according to the gas flow, so that the gas storage is controlled in a proper range, overhigh or overlow is avoided, the energy consumption of the system operation is reduced while the pollutants are efficiently treated, and the optimization of the system is achieved.
Further, the charging device adopts the principle of corona discharge, and charges are generated from the cavity outside the tube wall and then enter the tube to collide with particles such as dust/fog and the like for charging.
Further, the multi-force coupling pollutant removing device consists of a baffle plate and a discharge electrode between the baffle plate and the baffle plate, wherein the discharge electrode is connected with a high-voltage power supply.
As can be seen from fig. 1, the sensor 3 detects the pollutant generated in the production process, and transmits the detection signal to the intelligent control system 1, the intelligent control system 1 starts the #2 variable frequency circulating pump 15, the #1 high voltage power supply 11 and the #2 high voltage power supply 16, and the variable frequency induced draft fan 12 according to the signals, and simultaneously adjusts the frequencies of the circulating pump and the induced draft fan according to the intensity of the detection signal;
the gas containing pollutants is uniformly sucked into the multifunctional collecting cover 2, particles such as dust and fog in the gas collide with charges generated by the charging device 7 in the flue 4 and are agglomerated with atomized liquid drops generated by the spraying device 6 to realize agglomeration growth and partial removal of the dust and fog particles, water generated in the process is collected by the liquid drop collecting device 5 and then is sent back to the circulating filtering water tank 13 for filtering, and then is sent back to the spraying device 6 for recycling through the #2 variable-frequency circulating pump 15;
the pretreated gas enters a multi-force coupling removal tower 8, and the high-efficiency removal of pollutants in the gas is realized by utilizing the coupling of inertia force and electric field force in a multi-force coupling pollutant removal device 10, and then the gas is discharged through a variable-frequency induced draft fan 12; the water generated in the process is sent back to the circulating filtering water tank 13 for filtering through the bottom of the multi-force coupling removal tower 8 for use; in the operation process, under the control of the intelligent control system 1, the #1 circulating pump 14 is started periodically, and the multi-force coupling pollutant removing device 10 is cleaned by spraying through the cleaning nozzle 9 so as to eliminate particle deposition on the polar plate.
The above embodiments are provided to illustrate the technical concept and features of the present application and are intended to enable those skilled in the art to understand the content of the present application and implement the same, and are not intended to limit the scope of the present application. All equivalent changes or modifications made according to the spirit of the present application should be construed to be included in the scope of the present application.
Claims (8)
1. A garbage incinerator characterized by a housing having a flue gas inlet and a flue gas outlet; means for moving flue gas through the housing; means for directing the flue gas through the lower filter; an upper filter supported inside the housing at a position generally higher than the lower filter; means for directing the flue gas through the upper filter; each of the upper and lower filters includes a perforated sheet member positioned generally transverse to the flow of flue gas directed therethrough.
2. The incinerator according to claim 1, wherein said means for guiding flue gas through said lower filter is a lower baffle, said lower filter comprising a first lower filter member connected to one of the edge flanges and a second lower filter member connected to the other edge flange.
3. The incinerator according to claim 2 wherein said lower baffle has a pair of transverse end walls, each of said pair of transverse end walls being attached to said inlet duct.
4. A gas purification process for removing pollutants comprises a multifunctional efficient collecting cover and a multi-force coupling removing tower, wherein a sensor is arranged at an inlet at the bottom of the collecting cover, the sensor detects pollutants generated in the production process and transmits detection signals to an intelligent control system, the intelligent control system starts a #2 variable-frequency circulating pump, a #1 high-voltage power supply and a #2 high-voltage power supply according to the signals, and a variable-frequency induced draft fan, and meanwhile, the frequency of the circulating pump and/or the induced draft fan is adjusted according to the intensity of the detection signals;
the gas containing pollutants is uniformly sucked into a multifunctional collecting cover, particles such as dust/fog in the gas collide with charges generated by a charging device in a flue to be charged, collide with atomized liquid drops generated by a pretreatment nozzle to be agglomerated, grow and partially remove the dust/fog particles, water generated in the process is collected by the liquid drop collecting device and then is sent back to a circulating filtering water tank to be filtered, and then is sent back to the pretreatment nozzle for recycling through a #2 variable-frequency circulating pump;
and a flow sensor is arranged at the inlet at the bottom of the collecting cover, and the frequency of the fan is controlled according to the flow sensor.
5. The process for contaminant removal gas purification of claim 4, wherein the power of the variable frequency induced draft fan is controlled to increase when the detected flow rate increases, and the power of the variable frequency induced draft fan is controlled to decrease when the detected flow rate decreases.
6. The contaminant removal gas purification process according to claim 5, comprising a multifunctional efficient collection hood and a multi-force coupling removal tower, wherein the removal tower is connected with the collection hood through a pipeline, an air inlet groove is arranged at the lower part of the collection hood, an outlet pipeline is arranged at the upper part of the collection hood, a charging device, a spraying device and a liquid drop collecting device are arranged in the outlet pipeline, the charging device is arranged in a cavity on the wall of the outlet pipe, the spraying device is arranged at the upper part of the charging device, the collecting device is arranged at the lower part of the spraying device, and flue gas subjected to charging and spraying pretreatment enters the multi-force coupling removal tower; the device is characterized in that a cleaning nozzle and a multi-force coupling pollutant removal device are arranged in the removal tower, the cleaning nozzle is positioned at the upper part of the removal tower, the multi-force coupling pollutant removal device is positioned at the lower part of the cleaning nozzle, and the device comprises a plurality of baffle plates which are arranged at intervals and discharge electrodes arranged between adjacent baffle plates.
7. The process for purifying a contaminant removal gas according to claim 6, wherein a plurality of air inlet grooves are provided in a lower portion of the collecting hood, and the air inlet grooves have different widths, and the width of the air inlet grooves gradually increases in a direction from the center of the air inlet groove toward the side.
8. The process for purifying a contaminant removal gas according to claim 5, wherein in practice, the frequency control satisfies the relationship:
the maximum design speed of the inlet airflow at the bottom of the collecting cover is V, and the maximum frequency of the corresponding pump and fan is 50Hz, so that when the inlet airflow speed is V, the frequencies of the circulating pump and the fan are:
a× (V/V) ×50, where the coefficient a satisfies: a is more than or equal to 1 and less than or equal to 1.2.
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| CN202211400536.3A Active CN116857657B (en) | 2022-10-14 | 2022-11-09 | Garbage incinerator and purification process thereof |
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| CN115582381B (en) * | 2022-10-14 | 2024-05-24 | 山东大学 | Gas purifying device and process |
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| DE202014105711U1 (en) * | 2014-11-26 | 2014-12-02 | Zhewen Shi | Cleaning system for boiler flue gas |
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| US5143530A (en) * | 1990-10-22 | 1992-09-01 | Westinghouse Electric Corp. | Filtering apparatus |
| US5285737A (en) * | 1992-08-05 | 1994-02-15 | Tsai-Hsia Chen | Incinerator |
| US20020083691A1 (en) * | 2000-12-28 | 2002-07-04 | Li-Lin Chang | Oil filter device of smoke exhaust |
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| CN116808758B (en) | 2024-04-09 |
| CN116857657B (en) | 2024-04-09 |
| CN116808758A (en) | 2023-09-29 |
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