CN111536534A - High-temperature plasma organic waste liquid treatment shelter and treatment method - Google Patents
High-temperature plasma organic waste liquid treatment shelter and treatment method Download PDFInfo
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- CN111536534A CN111536534A CN202010490631.1A CN202010490631A CN111536534A CN 111536534 A CN111536534 A CN 111536534A CN 202010490631 A CN202010490631 A CN 202010490631A CN 111536534 A CN111536534 A CN 111536534A
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- melting furnace
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- 239000007788 liquid Substances 0.000 title claims abstract description 148
- 210000002381 Plasma Anatomy 0.000 title claims abstract description 84
- 239000010815 organic waste Substances 0.000 title claims abstract description 83
- 238000009272 plasma gasification Methods 0.000 claims abstract description 86
- 238000002844 melting Methods 0.000 claims abstract description 82
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 51
- 239000003546 flue gas Substances 0.000 claims abstract description 51
- 238000002485 combustion reaction Methods 0.000 claims abstract description 43
- 238000010791 quenching Methods 0.000 claims abstract description 31
- 239000002893 slag Substances 0.000 claims abstract description 31
- 230000000171 quenching Effects 0.000 claims abstract description 30
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims abstract description 25
- 239000000428 dust Substances 0.000 claims abstract description 23
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 20
- 238000002309 gasification Methods 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 81
- 235000010599 Verbascum thapsus Nutrition 0.000 claims description 45
- 239000002699 waste material Substances 0.000 claims description 45
- 239000007921 spray Substances 0.000 claims description 38
- 239000007789 gas Substances 0.000 claims description 36
- 239000000498 cooling water Substances 0.000 claims description 26
- 238000003860 storage Methods 0.000 claims description 25
- 238000009826 distribution Methods 0.000 claims description 18
- 239000000779 smoke Substances 0.000 claims description 18
- 238000004378 air conditioning Methods 0.000 claims description 13
- 239000002002 slurry Substances 0.000 claims description 13
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 9
- 235000011121 sodium hydroxide Nutrition 0.000 claims description 9
- 238000004140 cleaning Methods 0.000 claims description 8
- 239000008367 deionised water Substances 0.000 claims description 6
- 150000003384 small molecules Chemical class 0.000 claims description 6
- 238000011068 load Methods 0.000 claims description 4
- 238000011084 recovery Methods 0.000 claims description 4
- 238000005507 spraying Methods 0.000 claims description 4
- 230000003750 conditioning Effects 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 11
- 230000002829 reduced Effects 0.000 abstract description 10
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 abstract description 6
- 150000003839 salts Chemical class 0.000 abstract description 6
- 239000011780 sodium chloride Substances 0.000 abstract description 6
- 239000000126 substance Substances 0.000 abstract description 6
- 239000010881 fly ash Substances 0.000 abstract description 3
- 230000002588 toxic Effects 0.000 abstract description 3
- 231100000331 toxic Toxicity 0.000 abstract description 3
- 239000003513 alkali Substances 0.000 description 16
- 239000012530 fluid Substances 0.000 description 10
- 230000000087 stabilizing Effects 0.000 description 10
- 238000001816 cooling Methods 0.000 description 9
- 230000000694 effects Effects 0.000 description 9
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
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- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitrogen oxide Substances O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000004321 preservation Methods 0.000 description 2
- 238000000889 atomisation Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- VTVVPPOHYJJIJR-UHFFFAOYSA-N carbon dioxide;hydrate Chemical compound O.O=C=O VTVVPPOHYJJIJR-UHFFFAOYSA-N 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000000875 corresponding Effects 0.000 description 1
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- 238000010612 desalination reaction Methods 0.000 description 1
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- 239000011521 glass Substances 0.000 description 1
- 239000002920 hazardous waste Substances 0.000 description 1
- 231100000086 high toxicity Toxicity 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
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- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
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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
- F23G7/04—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste liquors, e.g. sulfite liquors
-
- 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
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
-
- 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
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
- F23G5/16—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
-
- 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
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/442—Waste feed arrangements
- F23G5/446—Waste feed arrangements for liquid waste
-
- 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
- F23G5/50—Control or safety arrangements
-
- 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
-
- 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
Abstract
The invention discloses a high-temperature plasma organic waste liquid treatment shelter and a treatment method, wherein the high-temperature plasma organic waste liquid treatment shelter comprises a shelter body and a treatment system; the cabin body is provided with a disposal area, and the disposal system is arranged in the disposal area of the cabin body; the disposal system comprises a liquid collecting tank, a discharge port of the liquid collecting tank is connected with a feed inlet of the plasma gasification melting furnace, a slag dragging device is arranged at a slag discharge port of the plasma gasification melting furnace, a flue gas outlet of the plasma gasification melting furnace is connected with a flue gas inlet of the secondary combustion chamber section, and the flue gas outlet of the secondary combustion chamber section is sequentially connected with a quenching deacidification tower, a dust remover, a hydroxyl generator and a chimney; according to the invention, the organic waste liquid is subjected to plasma gasification decomposition in a high-temperature reductive atmosphere, and dioxin is not generated in the gasification decomposition process; the generation of fly ash is avoided by arranging the slag dragging device; the salts in the organic waste liquid are collected in a centralized way after being sublimated at high temperature by utilizing the quenching deacidification tower and the dust remover, so that the secondary pollution is avoided, and the complete harmless treatment of toxic and harmful substances is realized.
Description
Technical Field
The invention belongs to the technical field of waste liquid treatment, and particularly relates to a high-temperature plasma organic waste liquid treatment shelter and a treatment method.
Background
The organic waste liquid is a common waste generated in the current industrial production activities, and generally, production enterprises are equipped with corresponding organic waste liquid disposal systems; but when an emergency happens, such as: the existing organic waste liquid disposal system is difficult to meet the application requirements in the aspects of damage of a centralized disposal system, waste liquid leakage or destruction of high-toxicity chemicals or drugs which are inconvenient to be merged into the centralized system for disposal; in this case, a compact, dedicated mobile organic waste liquid disposal system can effectively solve the problem.
At present, partial miniaturization and movable organic waste liquid disposal systems are applied to the fields, but the application effect is not ideal, and the main problems comprise: 1. the incineration method is mainly adopted, the treatment temperature is relatively low and is mostly 800-1100 ℃, and thorough harmless treatment cannot be realized; 2. the materials with high water content, such as waste liquid, are difficult to realize full combustion, and the secondary pollution is serious.
Disclosure of Invention
Aiming at the technical problems in the prior art, the invention provides a high-temperature plasma organic waste liquid treatment shelter and a treatment method thereof, and aims to solve the technical problems that the conventional mobile treatment system cannot realize thorough harmless treatment of organic waste liquid and is easy to cause secondary pollution.
In order to achieve the purpose, the invention adopts the technical scheme that:
the invention provides a high-temperature plasma organic waste liquid treatment shelter, which comprises a shelter body and a treatment system, wherein the disposal system comprises a first chamber and a second chamber; the cabin body is a cuboid-shaped shelter, a disposal area is arranged in the cabin body, and the disposal system is arranged in the disposal area of the cabin body;
the disposal system comprises a liquid collecting tank, a plasma gasification melting furnace, a slag dragging device, a secondary combustion chamber section, a quenching deacidification tower, a dust remover, a hydroxyl generator, an air compressor and a chimney;
the discharge hole of the liquid collecting tank is connected with the feed inlet of the plasma gasification melting furnace, and the slag dragging device is arranged at the slag discharge hole of the plasma gasification melting furnace; a smoke outlet of the plasma gasification melting furnace is connected with a smoke inlet of a second combustion chamber section, an air inlet of the second combustion chamber section is connected with an outlet of an air compressor, and a smoke outlet of the second combustion chamber section is connected with a smoke inlet of a quenching deacidification tower; the flue gas outlet of the quenching deacidification tower is connected with the flue gas inlet of the dust remover, the flue gas outlet of the dust remover is connected with the flue gas inlet of the hydroxyl generator, and the flue gas outlet of the hydroxyl generator is connected with the chimney.
Furthermore, the disposal system also comprises a waste liquid spray gun which is arranged between the liquid collecting tank and the plasma gasification melting furnace; one end of the waste liquid spray gun is connected with a discharge hole of the liquid collecting tank, the other end of the waste liquid spray gun is connected with a feed inlet of the plasma gasification melting furnace, and an air inlet of the waste liquid spray gun is connected with an outlet of the air compressor.
Further, the treatment system further comprises an air arc plasma torch arranged on the plasma gasification melting furnace and used for providing plasma jet; the air inlet of the air arc plasma torch is connected to the outlet of the air compressor.
Furthermore, the disposal system also comprises a water chilling unit and a cooling water tank, wherein the cooling water tank is used for loading deionized water; the cooling water tank comprises a first path of water inlet, a first path of water outlet, a second path of water inlet and a second path of water outlet, the first path of water outlet is connected with a cooling water inlet pipeline of the air arc plasma torch, and the first path of water inlet is connected with a water outlet pipeline of the air arc plasma torch; the second path of water inlet is connected with a cooling water outlet of the water chilling unit, and the second path of water outlet is connected with a water inlet of the water chilling unit.
Furthermore, the disposal system further comprises a burner and an oil storage tank, an outlet of the burner is connected with a port in the middle of the side surface of the plasma gasification melting furnace, and an oil outlet of the oil storage tank is connected with an oil inlet of the burner.
Further, the disposal system also comprises an induced draft fan; the induced draft fan is arranged between the hydroxyl generator and the chimney, one end of the induced draft fan is connected with the smoke outlet of the hydroxyl generator, and the other end of the induced draft fan is connected with the chimney.
Furthermore, the disposal system also comprises an alkali liquor storage tank, the alkali liquor storage tank is used for storing alkali liquor, and the outlet end of the alkali liquor storage tank is connected with a nozzle of the quenching deacidification tower.
Further, a control area is also arranged in the cabin body; the control area is an independent space and is provided with a heat-insulating wall surface; a control system is arranged in the control area; the control system comprises a power distribution cabinet, a control cabinet and a control console, the power distribution cabinet is connected with an external power supply, the power distribution cabinet is respectively connected with the disposal system, the control cabinet and the control console, one end of the control cabinet is connected with the disposal system, and the other end of the control cabinet is connected with the control console.
Further, the system also comprises a control area air conditioning system which is used for improving and adjusting the air environment of the control area; the control area air conditioning system comprises an air conditioner internal unit and an air conditioner external unit, wherein the air conditioner internal unit is arranged in the control area, and the air conditioner external unit is arranged in the disposal area.
The invention also provides a method for treating the high-temperature plasma organic waste liquid, which comprises the following steps:
collecting and storing the organic waste liquid to be treated by adopting a liquid collecting tank; starting the plasma gasification melting furnace to raise the temperature in the plasma gasification melting furnace to over 1200 ℃;
spraying the organic waste liquid to be treated in the liquid collection tank into a plasma gasification melting furnace for gasification decomposition reaction to obtain inorganic matter molten slurry and micromolecular gas; wherein the small molecule gas is CO or H2And CH4One or more of;
performing water quenching recovery on the inorganic matter molten slurry by adopting a slag dragging device;
introducing the micromolecule gas into the second combustion chamber section, and performing secondary combustion to obtain high-temperature flue gas;
after the high-temperature flue gas is subjected to quenching deacidification treatment, dedusting treatment and denitrification treatment in sequence, clean tail gas is obtained and is discharged through a chimney.
Compared with the prior art, the invention has the beneficial effects that:
the invention provides a high-temperature plasma organic waste liquid treatment shelter, which utilizes a plasma gasification melting furnace to carry out plasma gasification decomposition reaction on organic waste liquid, the gasification decomposition process does not depend on free radicals, organic matters in the organic waste liquid can be effectively decomposed, and the generation of dioxin is avoided; the slag fishing device is adopted to collect the inorganic matter molten slurry after gasification and decomposition, so that the generation of fly ash is avoided; through the arrangement of the second combustion chamber section, the quenching deacidification tower, the dust remover and the hydroxyl generator, the flue gas generated by gasification decomposition is subjected to deacidification, denitrification and salinity treatment, secondary pollution is avoided, the completely harmless treatment of toxic and harmful substances is realized, the volume reduction rate effect of organic matters is remarkable, the recycling degree is high, and the structure is simple; by arranging the treatment system in the cabin, mobile treatment is satisfied.
Furthermore, the waste liquid spray gun is adopted to realize the accurate measurement of the organic waste liquid entering the plasma gasification melting furnace, and the flow of the organic waste liquid can be accurately controlled; meanwhile, the waste liquid spray gun is adopted to atomize the organic waste liquid, so that the gasification and decomposition efficiency of the organic waste liquid in the plasma gasification melting furnace is improved, and the treatment difficulty and the total power consumption of the system are reduced.
Furthermore, the air arc plasma torch is used for providing high-temperature high-speed plasma jet flow, so that the formation of high-energy-density high-temperature reductive atmosphere in the plasma gasification melting furnace is ensured, harmful substances such as dioxin are prevented from being generated, and meanwhile, a large number of high-energy particles and reaction groups are provided, so that macromolecular organic matters in the organic waste liquid are rapidly decomposed into CO and CH under the high-energy-density high-temperature reductive atmosphere4、H2The low molecular gas effectively improves the gasification decomposition speed and the gasification decomposition efficiency of the organic waste liquid; by adopting the air arc plasma torch, the complexity of the air supply system is greatly simplified, and the volume of the whole treatment system is effectively reduced.
Furthermore, by arranging the cooling water tank and the water chilling unit, cooling water is adopted to exchange heat for the air arc plasma torch, and stable high-temperature and high-speed plasma jet flow output by the air arc plasma torch is ensured.
Furthermore, a burner is adopted to provide low energy density heat for the initial stage of baking the plasma gasification melting furnace, or partial energy is provided when the treatment capacity of the organic waste liquid to be treated is larger or the heat value of the treated object is lower, thereby realizing the auxiliary energy supply to the plasma gasification melting furnace.
Furthermore, through setting up the draught fan, for processing system and process flow provide aerodynamic, ensured the negative pressure environment of processing system, avoided the processing process by the revealing of handling thing and pollutant, avoided causing the possibility of personnel's infection, effectively prevented simultaneously that the plasma gasifies the danger that the interior pressure of melting furnace is too high and produces the explosion.
Furthermore, a control area with an independent space is adopted, a heat preservation wall is arranged, a power distribution cabinet, a control console and a plasma torch power cabinet are placed among the control area, damage to electric equipment due to weather can be prevented, an air conditioner is arranged in the control area, the adjustment of the temperature and the humidity of the environment in the control area is achieved, and the comfortable working environment of the electric equipment and personnel is guaranteed.
The invention also provides a high-temperature plasma organic waste liquid treatment method, which is characterized in that the organic waste liquid to be treated is stored in the liquid collecting tank in a centralized manner, so that the pollution of the organic waste liquid to the environment before treatment is avoided, the supply speed of the organic waste liquid in the treatment process is ensured, the stability of the treatment process is improved, and the treatment effect is ensured; organic matters in the organic waste liquid can be thoroughly gasified and decomposed in a high-energy-density high-temperature reducing atmosphere at the temperature of over 1200 ℃, the gasification and decomposition process does not depend on free radicals, and the generation of dioxin is avoided; after the inorganic matter molten slurry is subjected to water quenching treatment, a glass body is formed, and fly ash is avoided; carrying out secondary combustion on the gasified and decomposed small molecular gas to form high-temperature flue gas; the high-temperature flue gas is subjected to quenching deacidification treatment, dedusting treatment and denitrification treatment in sequence to obtain clean tail gas, so that the salt in the organic waste liquid is concentrated and collected after high-temperature sublimation, secondary pollution is avoided in the whole process, completely harmless treatment of toxic and harmful substances is realized, and the burning rate of organic matters is up to more than 99.99%.
In conclusion, the temperature plasma organic waste liquid treatment shelter and the treatment method can be simultaneously suitable for daily and emergency organic waste liquid treatment; by means of a high-temperature arc plasma technology, a disposal system can be customized and reasonably arranged for different types of organic waste liquid; by providing the treatment system and the control system in the rectangular parallelepiped shelter, the treatment system and the control system can be mounted on other vehicles such as a vehicle and a ship.
The square cabin for treating the warm plasma organic waste liquid and the treatment method have the characteristics of thorough treatment, high speed, high volume reduction rate and zero pollution, and realize the capacity of maneuvering and on-site treatment; the invention has ultrahigh volume reduction rate, and the volume reduction rate of the organic waste liquid can reach more than 99.99 percent; the disposal system has dual functions of high temperature and high activity, the gasification and decomposition reaction of the organic waste liquid is rapid, and the disposal speed is rapid; in the treatment process, the macromolecular organic matters are gasified into micromolecular gas, and dense smoke and peculiar smell are not generated; the salt in the organic waste liquid can be effectively recovered after sublimation; thorough treatment, complete realization of harmlessness, and no pollution to air, water sources and surrounding environment.
Drawings
FIG. 1 is a schematic view of the overall structure of an organic waste liquid disposal shelter according to the present invention;
FIG. 2 is a schematic view of the internal structure of the organic waste liquid disposal shelter according to the present invention;
FIG. 3 is a schematic view of the left front side structure of the disposal area in the organic waste liquid disposal shelter according to the present invention;
FIG. 4 is a schematic view of the left rear side structure of the disposal area in the organic waste liquid disposal shelter according to the present invention;
FIG. 5 is a schematic view of the right front side structure of the disposal area in the organic waste liquid disposal shelter according to the present invention;
FIG. 6 is a block diagram of the disposal area in the organic waste liquid disposal shelter according to the present invention.
Wherein, 1 cabin body, 2 disposal system, 3 control system, 4 control area air conditioning system; 11 treatment zone, 12 control zone; 21 liquid collecting tank, 22 waste liquid spray gun, 23 plasma gasification melting furnace, 24 air arc plasma torch, 25 slag fishing device, 26 burner, 27 second combustion chamber section, 28 quenching deacidification tower, 29 oil storage tank, 210 dust remover, 211 hydroxyl generator, 212 water chilling unit, 213 air compressor, 214 pressure stabilizing tank, 215 cooling water tank, 216 alkali liquor storage tank, 217 draught fan and 218 chimney; 31 a power distribution cabinet, 32 a control cabinet, 33 a plasma torch power supply and 34 a control console; 41 air-conditioning indoor unit and 42 air-conditioning outdoor unit.
Detailed Description
The present invention will be described in further detail with reference to specific embodiments.
As shown in the attached drawings 1-6, the invention provides a high-temperature plasma organic waste liquid treatment shelter, which comprises a shelter body 1, a treatment system 2, a control system 3 and a control area air conditioning system 4; the cabin body 1 is a cuboid-shaped shelter, and a top plate and side plates of the shelter are detachably connected; the treatment room 1 is provided with a treatment area 11 and a control area 12, the treatment system 2 is arranged in the treatment area 11 of the room 1, and the control system 3 is arranged in the control area 12 of the room 1; the disposal system 2 is used for carrying out innocent treatment on the organic waste liquid, and the control system 3 is connected with the disposal system 2 and is used for monitoring and controlling the disposal system 2; the control area 12 is an independent space, and the control area 12 is provided with a heat-insulating wall; the control zone air conditioning system 4 is used to condition the air environment of the control zone 12.
The disposal system 2 comprises a liquid collecting tank 21, a waste liquid spray gun 22, a plasma gasification melting furnace 23, an air arc plasma torch 24, a slag dragging device 25, a burner 26, a secondary combustion chamber section 27, a quenching deacidification tower 28, an oil storage tank 29, a dust remover 210, a hydroxyl generator 211, a water chilling unit 212, an air compressor 213, a pressure stabilizing tank 214, a cooling water tank 215, a lye storage tank 216, an induced draft fan 217 and a chimney 218.
The feed inlet of collection fluid reservoir 21 passes through the pipeline and is connected with organic waste liquid source, and collection fluid reservoir 21 is used for collecting the storage to the waste liquid of treating, and the discharge gate of collection fluid reservoir 21 and waste liquid spray gun 22's entrance point are connected, still are provided with the elevator pump between collection fluid reservoir 21 and the waste liquid spray gun 22, utilize the elevator pump to send the waste liquid pump of treating in the collection fluid reservoir 21 to waste liquid spray gun 22.
A waste liquid spray gun 22 is arranged above the plasma gasification melting furnace 23, and the outlet end of the waste liquid spray gun 22Is connected with the feed inlet of the plasma gasification melting furnace 23, and the air inlet of the waste liquid spray gun 22 is connected with the outlet of the air compressor 213; the organic waste liquid to be treated is atomized and sprayed into a plasma gasification melting furnace 23 through a waste liquid spray gun 22 to carry out plasma gasification decomposition reaction, so that micromolecular gas and inorganic matter molten slurry are obtained; wherein the small molecule gas is CO or H2And CH4One or more of them.
The air arc plasma torch 24 is arranged on the plasma gasification melting furnace 23 and is used for providing high-temperature high-speed plasma jet flow so as to form a high-energy-density high-temperature reductive reaction atmosphere in the plasma gasification melting furnace 23; the slag dragging device 25 is arranged below the plasma gasification melting furnace 23, a feed inlet of the slag dragging device 25 is connected with a slag discharge port of the plasma gasification melting furnace 23, and the slag dragging device 25 is used for performing water quenching collection on inorganic slag discharged from the plasma gasification melting furnace 23.
The burner 26 is arranged on the plasma gasification melting furnace 23, the outlet of the burner 26 is connected with the middle port of the side surface of the plasma gasification melting furnace 23, and the burner 26 is used for providing low-energy-density heat for the initial stage of baking the plasma gasification melting furnace 23, or providing partial energy when the treatment capacity of the organic waste liquid to be treated is large or the heat value of the treated object is low, so that auxiliary energy supply to the plasma gasification melting furnace 23 is realized; the oil inlet of the combustor 26 is connected with the oil outlet of the oil storage tank 29.
The flue gas outlet of the plasma gasification melting furnace 23 is connected with the flue gas inlet of the second combustion chamber section 27, and the second combustion chamber section 27 is used for carrying out secondary combustion on the micromolecule gas from the plasma gasification melting furnace 23; by arranging the secondary combustion chamber section 27, the space of the upper combustion area of the plasma gasification melting furnace is expanded, the processed substances and the small molecular gas generated by gasification decomposition are fully combusted, and the structural size of the plasma gasification melting furnace is effectively reduced; the flue gas outlet of the second combustion chamber section 27 is connected with the flue gas inlet of the rapid cooling deacidification tower 28, and the flue gas outlet of the rapid cooling deacidification tower 28 is connected with the flue gas inlet of the dust remover 210; the flue gas outlet of the dust remover 210 is connected with the flue gas inlet of the hydroxyl generator 211, and the flue gas outlet of the hydroxyl generator 211 is connected with the chimney 218; the induced draft fan 217 is arranged between the hydroxyl generator 211 and the chimney 218, one end of the induced draft fan 217 is connected with the smoke outlet of the hydroxyl generator 211, and the other end of the induced draft fan 217 is connected with the chimney 218.
The air compressor 213 is used for providing air for the waste liquid spray gun 22, the air arc plasma torch 24 and the second combustion chamber section 27, the outlet of the air compressor 213 is connected with the inlet of the surge tank 214, the surge tank 214 is used for stabilizing the pressure of the compressed air generated by the air compressor 213, the first outlet of the surge tank 214 is connected with the air inlet of the air arc plasma torch 24, the second outlet of the surge tank 214 is connected with the air inlet of the second combustion chamber section, and the third outlet of the surge tank 214 is connected with the air inlet of the waste liquid spray gun 22.
The cooling water tank 215 is used for loading deionized water, and the cooling water tank 215 comprises a first water inlet, a first water outlet, a second water inlet and a second water outlet; the first water outlet is connected with a cooling water inlet pipeline of the air arc plasma torch 24, and the first water inlet is connected with a water outlet pipeline of the air arc plasma torch 24; the second path of water inlet is connected with a cooling water outlet of the water chilling unit 212, and the second path of water outlet is connected with a water inlet of the water chilling unit 212; the water chilling unit 212 is used for cooling the deionized water, reducing the temperature of the water after heat exchange to a proper temperature, and introducing cooling water into the air arc plasma torch through the cooling water tank 215 for heat exchange, so that the air arc plasma torch 24 is ensured to keep a proper working temperature.
The lye storage tank 216 is used for storing lye, and the outlet end of the lye storage tank 216 is connected with a lye nozzle at the top of the quenching deacidification tower 28.
The control system 3 comprises a power distribution cabinet 31, a control cabinet 32, a control console 33 and a plasma torch power supply 34, the power distribution cabinet 31 is connected with an external power supply, the power distribution cabinet 31 is respectively connected with the treatment system 2, the control cabinet 32 and the control console 33, one end of the control cabinet 32 is connected with the treatment system 2, and the other end of the control cabinet 32 is connected with the control console 33; one end of the plasma torch power supply 34 is connected with the power distribution cabinet 31, the other end is connected with the air arc plasma torch, and the plasma torch power supply 34 is used for converting electric energy output by the power distribution cabinet into an electric energy form required by the air arc plasma torch.
The control cabinet 32 is connected to each device and instrument in the treatment system 2, and is configured to control and monitor a treatment operation state of each device and instrument in the treatment system 2, and the console 33 is connected to the control cabinet 32, and is configured to manually observe the operation state and input an operation instruction to the control cabinet 32.
The control area air conditioning system 4 comprises an air conditioner internal unit 41 and an air conditioner external unit 42, wherein the air conditioner internal unit 41 is installed in the control area 12, and the air conditioner external unit 42 is installed in the disposal area 11 and is used for improving and adjusting the air environment of the control area; the air conditioner internal unit 41 is used for regulating and controlling the temperature and humidity of the control area to ensure that electrical equipment and personnel are in a proper air environment, the air conditioner external unit 42 is arranged on the outer side of the heat preservation wall surface of the control area 12, and the air conditioner external unit 42 is arranged above the induced draft fan.
The invention also provides a method for treating the high-temperature plasma organic waste liquid, which comprises the following steps:
the treatment shelter is transported to a place needing to be treated, after the outer vertical surface and the top surface of the shelter body are removed, an external power supply cable, a water supply pipe and a water drainage pipe are connected, necessary detection is carried out, and the preparation work is completed;
collecting and storing the organic waste liquid to be treated by adopting a liquid collecting tank;
in the starting-up stage, an induced draft fan is opened to provide system aerodynamic force and a negative pressure environment;
the heat energy provided by the burner is utilized to dry the plasma gasification furnace, and the temperature in the gasification furnace is raised to 800 +/-50 ℃;
starting an air arc plasma torch to raise the temperature in the plasma gasification melting furnace to over 1200 ℃, and completing preparation work before treatment;
starting the plasma gasification melting furnace, atomizing and spraying the organic waste liquid to be treated in the liquid collection tank into the plasma gasification melting furnace, and carrying out plasma gasification decomposition reaction to obtain inorganic matter molten slurry and micromolecular gas; wherein the small molecule gas is one or more of CO, H2 and CH 4; the specific plasma gasification decomposition reaction comprises the following steps: gasifying and decomposing organic matters into CO, H2, CH4 and other small molecular gases, and moving the small molecular gases upwards under the action of a draught fan; evaporating water, sublimating salt and moving to the upper part along with the smoke; melting a small amount of inorganic matters at the bottom of the gasification melting furnace, and discharging the inorganic matters out of the plasma gasification melting furnace through a slag discharge port;
performing water quenching recovery on the inorganic matter molten slurry by adopting a slag dragging device;
the micromolecule gas enters the upper part and the second combustion chamber section of the plasma gasification melting furnace, and is mixed with compressed air generated by an air compressor for secondary combustion to obtain high-temperature flue gas, wherein the high-temperature flue gas is about 1000 ℃ flue gas and is formed by water vapor and CO2Mainly comprises the following steps of;
the high-temperature flue gas enters a quenching deacidification tower, and alkali liquor is sprayed out by an alkali liquor spray head on the quenching deacidification tower through quenching deacidification treatment, so that two functions are realized: firstly, rapidly reducing the temperature of high-temperature flue gas from 1000 ℃ to about 200 ℃ and avoiding a dioxin composite interval; secondly, alkali liquor reacts with a small amount of acid gas to remove the acid gas;
the flue gas after quenching and deacidification enters a bag-type dust remover to remove dust mixed in the flue gas;
the flue gas after dust removal enters a hydroxyl generator to remove residual organic matters with a small amount of odor and nitric oxides; and (4) obtaining clean tail gas, and sending the clean tail gas into a chimney through a draught fan to discharge the clean tail gas.
Compared with the existing movable organic waste liquid treatment shelter, the high-temperature plasma organic waste liquid treatment shelter and the treatment method provided by the invention have the advantages that the treatment is more thorough, the treatment efficiency is higher, the volume reduction rate is higher, the zero pollution discharge is realized, and the quick harmless maneuvering treatment capacity for organic waste liquid under daily and emergency conditions is met.
The plasma treatment technology used in the solid hazardous waste treatment process is miniaturized and specifically designed, and the treatment system is arranged in the cuboid-shaped shelter, so that the vehicle-mounted or ship-mounted movement is facilitated; the liquid collecting tank is used for storing and conveying the organic waste liquid to be treated in a centralized way, so that pollution before treatment is avoided; meanwhile, the processing speed can be stabilized, and the processing effect is ensured; a high-efficiency controllable waste liquid spray gun is adopted, and the flow of waste liquid is accurately controlled; the waste liquid spray gun is connected with 4-6 Bar compressed air, so that the atomization effect is optimal, the treatment effect is ensured, and the treatment difficulty and the total power consumption of the system are reduced; utilize high temperature to carry out water evaporation and salinity sublimation to through dust remover separation vapor and salinity, realize effective desalination, avoid the secondary to deal with.
Examples
The embodiment provides a high-temperature plasma organic waste liquid treatment shelter, which comprises a shelter body, a treatment system, a control system and a control area air conditioning system; the cabin body adopts a 40 ' HC container, the top plate and the side plate of the 40 ' HC container are both detachably connected, and the overall dimension of the 40 ' HC container is as follows: length × width × height 12000mm × 2400mm × 3000 mm; the cabin body is provided with a disposal area and a control area which are arranged in a separated way, and disposal equipment and other auxiliary equipment are mainly placed in the disposal area; the control area is in a room form, the control area is provided with an independent space, the control area is provided with a heat-insulating wall, electric equipment and control equipment are mainly placed in the control area, and meanwhile, the work and rest areas of operators are provided.
In this embodiment, the disposal system is installed in a disposal area of the cabin, the control system is disposed in a control area of the cabin, the disposal system is used for performing innocent treatment on the organic waste liquid, and the control system is connected with the disposal system and is used for performing control operation on the disposal system; the control area air conditioning system is installed in the control area for adjusting an air environment of the control area.
The disposal system comprises a liquid collecting tank, a waste liquid spray gun, a plasma gasification melting furnace, an air arc plasma torch, a slag fishing device, a diesel oil burner, a secondary combustion chamber section, a quenching deacidification tower, a diesel oil storage tank, a bag-type dust remover, a hydroxyl generator, a water chilling unit, an air compressor, a pressure stabilizing tank, a cooling water tank, an alkali liquor storage tank, an induced draft fan and a chimney.
The feed inlet of collection fluid reservoir passes through the pipeline and is connected with organic waste liquid source, and collection fluid reservoir is used for collecting the storage to the pending waste liquid, and the discharge gate of collection fluid reservoir and the entrance connection of waste liquid spray gun still are provided with the elevator pump between collection fluid reservoir and the waste liquid spray gun, utilize the elevator pump to send to the waste liquid spray gun the pending waste liquid in the collection fluid reservoir. Waste liquid spray gun arrangementThe outlet end of the waste liquid spray gun is connected with the feed inlet of the plasma gasification melting furnace above the plasma gasification melting furnace, and the air inlet of the waste liquid spray gun is connected with the outlet of the air compressor; atomizing the organic waste liquid to be treated into a plasma gasification melting furnace through a waste liquid spray gun, and carrying out plasma gasification decomposition reaction to obtain micromolecular gas and inorganic matter molten slurry; wherein the small molecule gas is CO or H2And CH4One or more of them.
The air arc plasma torch is arranged on the plasma gasification melting furnace and used for providing high-temperature high-speed plasma jet flow, a plasma gasification decomposition process and forming a high-energy-density high-temperature reducing atmosphere at 1200-1600 ℃ in the plasma gasification melting furnace; the slag dragging device is arranged at a slag outlet below the plasma gasification melting furnace, a feed inlet of the slag dragging device is connected with a slag outlet of the plasma gasification melting furnace, and the slag dragging device is used for performing water quenching collection on inorganic slag.
The diesel combustion engine is arranged on the plasma gasification melting furnace, an outlet of the diesel combustion engine is connected with a port in the middle of the side surface of the plasma gasification melting furnace, and the diesel combustion engine is used for providing low-energy-density heat for the initial stage of baking the plasma gasification melting furnace, or providing partial energy when the treatment capacity of the organic waste liquid to be treated is large or the heat value of the treated object is low, so that auxiliary energy supply to the plasma gasification melting furnace is realized; an oil inlet of the diesel oil burner is connected with the diesel oil storage tank.
A smoke outlet of the plasma gasification melting furnace is connected with a smoke inlet of a second combustion chamber section, and the second combustion chamber section is used for carrying out secondary combustion on the micromolecule gas; the flue gas outlet of the second combustion chamber section is connected with the flue gas inlet of the rapid cooling deacidification tower, and the flue gas outlet of the rapid cooling deacidification tower is connected with the flue gas inlet of the bag-type dust remover; the smoke outlet of the bag-type dust collector is connected with the smoke inlet of the hydroxyl generator, and the smoke outlet of the hydroxyl generator is connected with the chimney; the induced draft fan is arranged between the hydroxyl generator and the chimney, one end of the induced draft fan is connected with the hydroxyl generator, and the other end of the induced draft fan is connected with the chimney.
The air compressor is used for providing air for the waste liquid spray gun, the air arc plasma torch and the secondary combustion chamber section, the outlet of the air compressor is connected with the inlet of the pressure stabilizing tank, the pressure stabilizing tank is used for stabilizing the pressure of the compressed air generated by the air compressor, the first outlet of the pressure stabilizing tank is connected with the air inlet of the air arc plasma torch, and the second outlet of the pressure stabilizing tank is connected with the air inlet of the secondary combustion chamber section; and a third outlet of the pressure stabilizing tank is connected with an air inlet of the waste liquid spray gun.
The cooling water tank is used for loading deionized water and comprises a first path of water inlet, a first path of water outlet, a second path of water inlet and a second path of water outlet; the first water outlet is connected with a cooling water inlet pipeline of the air arc plasma torch, and the first water inlet is connected with a water outlet pipeline of the air arc plasma torch; the second path of water inlet is connected with a cooling water outlet of the water chilling unit, and the second path of water outlet is connected with a water inlet of the water chilling unit; the water chilling unit is used for cooling the deionized water, the temperature of the water after heat exchange is reduced to a proper temperature, and the cooling water is introduced into the air arc plasma torch through the cooling water tank for heat exchange, so that the air arc plasma torch is ensured to keep a proper working temperature.
The alkali liquor storage tank is used for storing alkali liquor, and the outlet end of the alkali liquor storage tank is connected with the top alkali liquor nozzle of the quenching deacidification tower.
The control system comprises a power distribution cabinet, a control console and a plasma torch power supply, wherein the power distribution cabinet is connected with an external power supply, the power distribution cabinet is respectively connected with the treatment system, the control cabinet and the control console, one end of the control cabinet is connected with the treatment system, and the other end of the control cabinet is connected with the control console; one end of the plasma torch power supply is connected with the power distribution cabinet, the other end of the plasma torch power supply is connected with the air arc plasma torch, and the plasma torch power supply is used for converting electric energy output by the power distribution cabinet into an electric energy form required by the air arc plasma torch.
The control area air conditioning system comprises an air conditioner internal unit and an air conditioner external unit, wherein the air conditioner internal unit is arranged in the control area, and the air conditioner external unit is arranged in the disposal area and is used for improving and adjusting the air environment of the control area.
The embodiment also provides a method for treating the high-temperature plasma organic waste liquid, which comprises the following steps:
(1) the treatment shelter is transported to a place needing to be treated, after a top plate and a side plate of the shelter body are removed, an external power supply cable, a water supply pipe and a water drainage pipe are connected with the treatment shelter, necessary detection is carried out, and preparation work is completed;
(2) collecting and storing the organic waste liquid to be treated by using a liquid collection tank;
(3) starting the plasma gasification melting furnace, and opening the induced draft fan to provide aerodynamic force and a negative pressure environment for the disposal system in a starting-up stage;
(4) providing heat energy by using a diesel combustion engine to dry the plasma gasification melting furnace, and raising the temperature in the plasma gasification melting furnace to 800 +/-50 ℃;
(5) starting an air arc plasma torch, raising the temperature in the plasma gasification melting furnace to over 1200 ℃, and completing preparation work before treatment;
(6) pumping the organic waste liquid to be treated in the liquid collecting tank to a waste liquid spray gun by using a lift pump, atomizing by using the waste liquid spray gun, and spraying the atomized liquid into a plasma gasification melting furnace for gasification decomposition reaction; the organic waste liquid completes the following reactions in the lower part of the plasma gasification melting furnace: gasifying and decomposing organic matters into CO, H2, CH4 and other small molecular gases, and moving the small molecular gases upwards to a flue gas outlet of a plasma gasification melting furnace under the action of a draught fan; evaporating water, sublimating salt and moving to an eyeball outlet of the plasma gasification melting furnace along with the micromolecular gas; melting a small amount of inorganic matters at the bottom of the plasma gasification melting furnace to form inorganic matter molten slurry, and discharging the inorganic matter molten slurry through a slag discharge port of the plasma gasification melting furnace;
(7) the inorganic matter molten slurry is discharged from a slag discharge port and then enters a slag dragging device for water quenching recovery;
(8) the small molecule gas enters the second combustion chamber section through a flue gas outlet at the upper part of the plasma gasification melting furnace, and is subjected to secondary combustion with compressed air generated by an air compressor in the second combustion chamber section to form steam and CO2High-temperature flue gas at 1000 ℃ mainly;
(9) the alkali liquor in the alkali liquor storage tank is sprayed into the rapid cooling deacidification tower through a spray head, and the rapid cooling and deacidification treatment is realized after the high-temperature flue gas enters the rapid cooling deacidification tower; specifically, firstly, the high-temperature flue gas is quickly reduced from 1000 ℃ to 200 ℃ to avoid a dioxin compounding interval; secondly, reacting the alkali liquor with a small amount of acid gas to remove acid in the flue gas;
(10) the flue gas after quenching and deacidification enters a bag-type dust remover to remove dust and salt contained in the flue gas;
(11) the flue gas after dust removal enters a hydroxyl generator to remove residual organic matters with a small amount of odor and nitrogen oxides, so that the denitrification of the flue gas is realized, and clean tail gas is obtained;
(12) the clean tail gas is sent into a chimney through a draught fan and is discharged.
According to the high-temperature plasma organic waste liquid treatment shelter and the treatment method, a high-temperature arc plasma technology is adopted, so that the high-temperature plasma organic waste liquid treatment shelter has the advantages of high treatment temperature, oxygen-deficient treatment atmosphere, high reaction speed, high degree of harmlessness and the like, and the problems of incomplete harmlessness and serious secondary pollution of the conventional system can be effectively solved.
The above description is only illustrative of the preferred embodiments of the present invention, and any structural changes, improvements, modifications, etc. made without departing from the principle of the present invention are deemed to be within the scope of the present invention.
Claims (10)
1. The high-temperature plasma organic waste liquid treatment shelter is characterized by comprising a shelter body (1) and a treatment system (2); the cabin body (1) is a cuboid-shaped shelter, a treatment area (11) is arranged in the cabin body (1), and the treatment system (2) is arranged in the treatment area (11) of the cabin body (1);
the disposal system (2) comprises a liquid collecting tank (21), a plasma gasification melting furnace (23), a slag dragging device (25), a secondary combustion chamber section (27), a quenching deacidification tower (28), a dust remover (210), a hydroxyl generator (211), an air compressor (213) and a chimney (218);
a discharge hole of the liquid collecting tank (21) is connected with a feed inlet of the plasma gasification melting furnace (23), and the slag dragging device (25) is arranged at a slag discharge hole of the plasma gasification melting furnace (23); a smoke outlet of the plasma gasification melting furnace (23) is connected with a smoke inlet of a second combustion chamber section (27), an air inlet of the second combustion chamber section (27) is connected with an outlet of an air compressor (213), and a smoke outlet of the second combustion chamber section (27) is connected with a smoke inlet of a quenching deacidification tower (28); the flue gas outlet of the quenching deacidification tower (28) is connected with the flue gas inlet of the dust remover (210), the flue gas outlet of the dust remover (210) is connected with the flue gas inlet of the hydroxyl generator (211), and the flue gas outlet of the hydroxyl generator (211) is connected with the chimney (218).
2. A high temperature plasma organic waste liquid treatment shelter as claimed in claim 1, characterized in that the treatment system (2) further comprises a waste liquid spray gun (22), the waste liquid spray gun (22) is arranged between the liquid collecting tank (21) and the plasma gasification melting furnace (23); one end of the waste liquid spray gun (22) is connected with the discharge hole of the liquid collecting tank (21), the other end of the waste liquid spray gun (22) is connected with the feed hole of the plasma gasification melting furnace (23), and the air inlet of the waste liquid spray gun (22) is connected with the outlet of the air compressor (213).
3. A high temperature plasma organic waste solution treatment shelter as claimed in claim 1, characterized in that the treatment system (2) further comprises an air arc plasma torch (24), the air arc plasma torch (24) being arranged on the plasma gasification melting furnace (23) for providing a plasma jet; the air inlet of the air arc plasma torch (24) is connected to the outlet of the air compressor (213).
4. A high temperature plasma organic waste liquid treatment shelter as claimed in claim 3, wherein the treatment system (2) further comprises a water chiller (212) and a cooling water tank (215), the cooling water tank (215) is used for loading deionized water; the cooling water tank (215) comprises a first water inlet, a first water outlet, a second water inlet and a second water outlet, the first water outlet is connected with a cooling water inlet pipeline of the air arc plasma torch (24), and the first water inlet is connected with a water outlet pipeline of the air arc plasma torch (24); the second path of water inlet is connected with a cooling water outlet of the water chilling unit (212), and the second path of water outlet is connected with a water inlet of the water chilling unit (212).
5. A high temperature plasma organic waste liquid treatment shelter as claimed in claim 1, characterized in that the treatment system (2) further comprises a burner (26) and an oil storage tank (29), the outlet of the burner (26) is connected with the side middle port of the plasma gasification melting furnace (23), and the oil outlet of the oil storage tank (29) is connected with the oil inlet of the burner (26).
6. A high temperature plasma organic waste treatment shelter as claimed in claim 1, wherein the treatment system (2) further comprises an induced draft fan (217); the induced draft fan (217) is arranged between the hydroxyl generator (211) and the chimney (218), one end of the induced draft fan (217) is connected with the smoke outlet of the hydroxyl generator (211), and the other end of the induced draft fan (217) is connected with the chimney (218).
7. A high temperature plasma organic waste solution treatment shelter as claimed in claim 1, characterized in that the treatment system (2) further comprises a lye storage tank (216), the lye storage tank (216) is used for storing lye, the outlet end of the lye storage tank (216) is connected with the nozzle of the quench deacidification tower (28).
8. A high temperature plasma organic waste liquid treatment shelter as claimed in claim 1, wherein the shelter body (1) is further provided with a control area (12); the control area (12) is an independent space, and the control area (12) is provided with a heat-insulating wall surface; a control system (3) is arranged in the control area (12); the control system (3) comprises a power distribution cabinet (31), a control cabinet (32) and a control console (33), the power distribution cabinet (31) is connected with an external power supply, the power distribution cabinet (31) is respectively connected with the treatment system (2), the control cabinet (32) and the control console (33), one end of the control cabinet (32) is connected with the treatment system (2), and the other end of the control cabinet is connected with the control console (33).
9. A high temperature plasma organic waste liquid treatment shelter as claimed in claim 8, further comprising a control area air conditioning system (4) for improved conditioning of the air environment of the control area; the control area air conditioning system comprises an air conditioner internal unit (41) and an air conditioner external unit (42), wherein the air conditioner internal unit (41) is installed in the control area (12), and the air conditioner external unit (42) is installed in the disposal area (11).
10. A method for treating high temperature plasma organic waste liquid, which is characterized in that the high temperature plasma organic waste liquid treatment square cabin of any one of claims 1-9 is used, and comprises the following steps:
collecting and storing the organic waste liquid to be treated by adopting a liquid collecting tank; starting the plasma gasification melting furnace to raise the temperature in the plasma gasification melting furnace to over 1200 ℃;
spraying the organic waste liquid to be treated in the liquid collection tank into a plasma gasification melting furnace for gasification decomposition reaction to obtain inorganic matter molten slurry and micromolecular gas; wherein the small molecule gas is CO or H2And CH4One or more of;
performing water quenching recovery on the inorganic matter molten slurry by adopting a slag dragging device;
introducing the micromolecule gas into the second combustion chamber section, and performing secondary combustion to obtain high-temperature flue gas;
after the high-temperature flue gas is subjected to quenching deacidification treatment, dedusting treatment and denitrification treatment in sequence, clean tail gas is obtained and is discharged through a chimney.
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| CN202010490631.1A CN111536534A (en) | 2020-06-02 | 2020-06-02 | High-temperature plasma organic waste liquid treatment shelter and treatment method |
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| CN202010490631.1A CN111536534A (en) | 2020-06-02 | 2020-06-02 | High-temperature plasma organic waste liquid treatment shelter and treatment method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114392570A (en) * | 2022-02-09 | 2022-04-26 | 上海翰逸环保科技有限公司 | Cutting fluid oil atomization microwave plasma treatment device and treatment process thereof |
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2020
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114392570A (en) * | 2022-02-09 | 2022-04-26 | 上海翰逸环保科技有限公司 | Cutting fluid oil atomization microwave plasma treatment device and treatment process thereof |
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