CN116678002A - Hazardous waste sludge high-temperature melting pyrolysis flue gas quality-separating recovery device - Google Patents
Hazardous waste sludge high-temperature melting pyrolysis flue gas quality-separating recovery device Download PDFInfo
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- CN116678002A CN116678002A CN202310474884.3A CN202310474884A CN116678002A CN 116678002 A CN116678002 A CN 116678002A CN 202310474884 A CN202310474884 A CN 202310474884A CN 116678002 A CN116678002 A CN 116678002A
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- 230000008018 melting Effects 0.000 title claims abstract description 101
- 238000002844 melting Methods 0.000 title claims abstract description 100
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 77
- 239000003546 flue gas Substances 0.000 title claims abstract description 77
- 239000002920 hazardous waste Substances 0.000 title claims abstract description 54
- 238000000197 pyrolysis Methods 0.000 title claims abstract description 40
- 238000011084 recovery Methods 0.000 title claims abstract description 23
- 239000002893 slag Substances 0.000 claims abstract description 153
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- 229910052782 aluminium Inorganic materials 0.000 description 2
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- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
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- 230000010534 mechanism of action Effects 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
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- 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
- F23G5/10—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating electric
-
- 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
-
- 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
- F23G5/46—Recuperation of heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2202/00—Combustion
- F23G2202/10—Combustion in two or more stages
- F23G2202/102—Combustion in two or more stages with supplementary heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2202/00—Combustion
- F23G2202/20—Combustion to temperatures melting waste
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2204/00—Supplementary heating arrangements
- F23G2204/20—Supplementary heating arrangements using electric energy
- F23G2204/204—Induction
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/10—Waste heat recuperation reintroducing the heat in the same process, e.g. for predrying
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/12—Sludge, slurries or mixtures of liquids
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/40—Valorisation of by-products of wastewater, sewage or sludge processing
Abstract
The invention discloses a high-temperature melting pyrolysis flue gas quality recovery device for hazardous waste sludge, which solves the problems of how to efficiently collect and dispose pyrolysis flue gas and recycling the pyrolysis flue gas in the existing device for recycling heavy metals from hazardous waste sludge. The technical scheme includes that the furnace body provided with an induction coil and a crucible is arranged in the furnace body, a feed pipe and a primary flue gas collecting hood are arranged at the top of the furnace body, a slag outlet is arranged on the side wall of the furnace body, a slag chute is arranged below the outer side of the slag outlet, and an annular gas collecting hood taking the slag outlet as the center is arranged above the slag chute; the annular gas collecting hood consists of an inner ring gas collecting hood and an outer ring gas collecting hood, wherein the inner ring gas collecting hood is connected with a secondary gas flue, and the outer ring gas collecting hood is connected with a tertiary gas flue. The invention has the advantages of simple structure, high heat efficiency, cleanness, environmental protection, stability, high efficiency, controllable components, high recovery rate of heavy metal components and continuous production.
Description
Technical Field
The invention belongs to the field of hazardous waste treatment, relates to hazardous waste high-temperature melting pyrolysis flue gas collection and waste heat and residual energy recycling, and particularly relates to a hazardous waste sludge high-temperature melting pyrolysis flue gas quality-classifying recycling device for heavy metal component recycling.
Background
The internationally popular treatment modes of hazardous waste sludge are as follows: a melting solidification treatment, a cement coagulation solidification treatment, a medicament treatment and an acid solution leaching treatment. Among them, the most studied ones are the melt-solidification treatment techniques, which are most favored in developed countries such as the united states, germany, japan, etc. The sludge is subjected to innocent treatment in a melting mode, a glass body structure formed by melting and solidification can effectively fix heavy metals, organic compounds, dioxin and other toxic components in the sludge can be decomposed by utilizing high temperature (more than 1500 ℃) to prevent the harmful components from damaging the ecological environment, and the obtained glass slag product can be further recycled, so that the high-temperature melting treatment is widely paid attention to [ money Yuan Dong, ma Zengyi, zhang Yike and the like ] in the innocent treatment of heavy metal hazardous waste.
Melting furnaces currently used in the field of hazardous waste disposal mainly include resistive melting furnaces and plasma melting furnaces. The resistance type melting furnace generally inserts or contacts electrodes into materials, and utilizes the difference between the anode and the cathode of different electrodes to realize current passing by taking the melted materials as media. When current passes through the molten material, heat is generated due to the self-resistance effect of the material, and the temperature of the material is increased to realize high-temperature melting.
The plasma melting furnace utilizes electric energy to excite a plasma torch to generate high-temperature plasma. The high-temperature plasma generates high temperature in the closed melting furnace, materials are melted and treated, slag becomes a glassy product after water quenching, heavy metals are effectively solidified, the leaching rate is extremely low, and the recycling utilization of the building material fields such as roadbed aggregates, sand/pebbles/gravels for construction, cement aggregates, concrete admixture and the like can be realized.
The us was earlier than 1986 in the use of thermal plasma fusion technology to simulate the treatment of radioactive nuclear waste, and to date many thermal plasma fusion treatment plants have been built to treat various hazardous wastes including waste incineration fly ash. Switzerland used the Retech's PACT technology to treat hazardous waste in 1990, and was independently developed by DAE science and technology company in 1998 to successfully produce a thermal plasma generation system which is applied to the melting treatment of various hazardous wastes including waste incineration fly ash. Other countries such as plasma spray gun technology developed by Europlasta company in France, 24t day treatment plasma melting furnace built by Resorotion Canda Limited in Canada, 5.5 ten thousand tons/year plasma melting furnace built by Scan Dust company in Sweden and B.U.S, direct current plasma melting technology successfully developed in 1990 in England, PLASSON plasma melting technology developed by STL Limited in Australia and PGM technology applied and developed by EER in Israel all show the advantages of high capacity reduction rate, thorough dioxin removal, effective heavy metal separation and the like of the plasma high-temperature melting technology. In addition, nishida and the like take household garbage incineration fly ash as an example, the properties of the glass body material produced by melting are quite stable, the removal rate of dioxin is up to 99.9%, and the leaching property of heavy metals also accords with the toxic leaching standard. The fused glass residue is crushed and used as cement and asphalt mixture or made into water permeable bricks, etc., and has certain practical value.
The study of the field of high-temperature melting treatment of wastes is earlier and a series of policy and regulation are issued. In 2009, heavy metal leaching of a molten product was restricted in japan by the handbook of industrial waste melt disposal product quality control, and the total amount of heavy metal was restricted when the molten product was used as a roadbed material. The leaching and total leaching amount of heavy metals are listed as strict limit indexes, wherein the limit of six chromium leaching reaches 0.05mg/L at the maximum, the limit of total mercury leaching is only 0.0005mg/L, 122 sets of garbage gasification melting units which are put into operation in Japan in 2013 are reached, and the annual treatment capacity reaches 691.6 ten thousand tons. Ash residues obtained after the garbage is gasified enter a melting area at the bottom of the gasifier. The reaction of oxygen-enriched air, coke and combustible components in garbage can provide heat energy, and the temperature of ash fusion area can reach 1800 ℃. The slag is obtained after the melting of inorganic components, metals and the like in the slag and the water quenching treatment, harmful heavy metals are wrapped in a vitreous structure, and the heavy metal leaching meets the relevant standards. The molten slag material has good performance, and can be used as a filling material of a capital construction [ Yang Junbo, li Jun, su Mingzhou, etc. ] Japanese garbage gasification treatment technology is discussed, green technology is 2016 (2): 146-147 ].
Three sludge melting furnaces are built in Fushan county, japan. The sludge is treated by a dryer until the water content is 20%, and then enters a surface melting furnace for high-temperature melting treatment at 1300 ℃. The slag has good water permeability and proper strength, and is mainly used as auxiliary materials of water pipe materials, roadbed materials or asphalt mixtures.
Swiss gasification melting technology was introduced by Kawasaki iron production in Japan, and a 2-seat 150t/d melting furnace was constructed in Japanese Qianye. Oxygen is blown into the furnace body from the bottom to react with combustible components in the materials to release heat, so that metal and inorganic components in the solid waste are melted. The melting center temperature reached 2000 ℃. After the materials are melted, the materials flow into a homogenizing furnace at 1600 ℃ for heat preservation and homogenizing distribution, and then the molten glass slag is obtained through cooling by a water quenching system. Pb, cd, hg and the like in the molten slag obtained by the system meet the soil emission standard, and the residue can be used as roadbed materials [ Tan Tiepeng ], japanese sewage sludge melting treatment and furnace dust building material resource ratio, environmental science and technology, 1996 (1): 87-92 ].
The domestic hazardous waste melting technology research has been carried out later in the century, such as Zhao Guangjie, and the like, to develop experimental researches on electric heating type melting and solidifying waste incineration fly ash by adopting a rapid heating tube furnaceThe corundum disc filled with fly ash is put into a furnace, and the fly ash in the furnace is heated by a power supply. The maximum working temperature of the tube furnace is 1600 ℃, and the maximum heating rate is 20 ℃/min. Experiments show that the fly ash starts to melt at about 1200 ℃ and becomes liquid phase at about 1290 ℃ and can flow [ Zhao Guangjie, li Haibin, zhao Zengli, and the like ], the experimental study of the electrothermal melting and solidifying the waste incineration fly ash, renewable energy sources, 2005.5 (total 123 st stage): 44-46 ]. Pilot-scale melting treatment of dangerous waste incineration ash slag by Hu Ming team with a plasma melting furnace indicates that the submerged arc and the open arc have little influence on the components and the crystal structure of the slag, the leaching of heavy metals in the slag is lower than the national standard limit value, the secondary fly ash generation rate is 7.5%, and the main components of the secondary fly ash are NaCl [ Hu Ming, tiger training, shao Zheru, and the like. Zhou the effect of additives on the melting of waste SCR catalysts was investigated. When the mass fraction of the additive was 40% (Fe 2 O 3 、SiO 2 CaO and Al 2 O 3 The mass fractions of the slag are 31.2%, 2.64%, 5.2% and 0.96%, and the leaching mass concentrations of heavy metals Ni, as, se, cu and Mn in the slag are respectively reduced by 98.6%, 68.0%, 96.8%, 11.1% and 77.3% [ Zhou, guohuantao, zhou Mingxi. The influence of different additives on the melting harmless treatment of the waste SCR catalyst. Programming journal, 2017 (12): 999-1006 ]. Liu Jinhe et al, by employing a gasification melting process to dispose of the engineering application of the integrated hazardous waste, the results demonstrate that: the process has the advantages of low fuel consumption, low smoke amount, low fly ash production amount, low dioxin, low hot burning rate, no need of landfill of the final vitrified products and the like; the emission values of ash burning rate, smoke pollutants (including NOx, dioxin and the like) and the like all meet the hazardous waste incineration pollution control standard; the vitreous content, acid dissolution rate, heavy metal leaching toxicity and the like of the vitrified product formed by high-temperature melting of gasified ash meet the technical requirements of vitrified products for solid wastes, no need of landfill and recycling [ Liu Jinhe, ma Mingshui, wang Mingfei ] the application of gasification and melting process to the treatment of dangerous wastes, environmental science and technology 2022,35 (02): 47-51 ]. Liu Xin et al studied the mechanism of action of thermal plasma melting vitrification and were mainlyThe influence factors are that the fly ash is vitrified and melted by the thermal plasma, and the research discovers that the heavy metal in the fly ash is effectively solidified, toxic and harmful organic matters are effectively decomposed, and the fly ash slag has compact structure and good recycling potential. But Cl - The problem of high corrosion and energy consumption is still a problem to be solved in the industrial utilization process of the plasma fly ash fusion technology [ Liu Xin, li Zhe, li Juanjuan ] the application of the thermal plasma technology in fly ash fusion treatment, coal and chemical industry 2022,45 (11): 158-160 ]. Wang Weiming and the like, the invention discloses a high-temperature melting treatment method of household garbage incineration fly ash of synergistic sludge and aluminum ash, which comprises the steps of pretreating the household garbage incineration fly ash, the aluminum ash and the sludge, simultaneously controlling the water content, carrying out high-temperature gasification melting treatment in a melting furnace, quenching and molding after tempering in a slag tempering furnace, carrying out combustion treatment in a secondary combustion chamber, and finally carrying out flue gas purification, secondary fly ash treatment and recycling.
Tian Yanjin and the like, the hazardous waste incinerator slag is subjected to a melting test, the melting temperature is 1350 ℃, and the melting time is 30min. Research results show that the molten slag has a good solidification effect on heavy metals, but the heavy metals are one of important limiting factors for recycling the slag [ Tian Yanjin, su Xiufeng, sun Zhenguo, and the like ], research on melting and recycling the hazardous waste incineration slag, china resource comprehensive utilization. 2021,39 (05): 21-23 ], so that the efficient separation of the heavy metals in the hazardous waste can effectively widen the recycling way of the molten slag.
The above researches fully demonstrate that the recycling of the hazardous waste sludge can be effectively realized by carrying out the melting treatment of the hazardous waste sludge, and the waste is changed into valuable. Meanwhile, researches also show that if the heavy metal components in the hazardous waste sludge can be efficiently separated, the additional value of recycling of the hazardous waste sludge can be greatly improved.
In order to efficiently recycle metals/heavy metals in the hazardous waste sludge, the intermediate frequency induction furnace widely used in the metallurgical industry is transplanted to the harmless and recycling treatment process of the hazardous waste sludge by the industry personnel. As a key smelting device commonly adopted in the casting industry in China, the medium frequency induction furnace has the advantages of low investment, quick return, high heat efficiency, cleanness, environmental protection, stability, high efficiency, controllable components and the like [ Li, zhang Lele, tong and the like ], the medium frequency induction furnace is used for selecting a structure and discussing an electricity-saving way, and is used for industrial heating, 2022,51 (6): 7-9,19 ]
However, because of the complex components of the hazardous waste sludge, the contradiction exists between the melting speed of the hazardous waste sludge and the escape speed of volatile matters contained in the sludge in the actual production process; meanwhile, in order to realize recovery of heavy metals in the hazardous waste sludge, a certain amount of reducing components are doped in heavy metal hazardous waste, the reducing components are volatilized in the melting pyrolysis process, and the volatilization speed is asynchronous with the melting speed of the hazardous waste sludge, so that the problems of capturing and recycling pyrolysis smoke exist in the hazardous waste sludge melting treatment process.
The pyrolysis flue gas contains a large amount of organic pollutants and dioxin pollutants, and if such flue dust is not fully collected and improperly treated, serious pollution is caused to the environment, and great occupational hazard is brought to personnel at disposal. Therefore, how to collect and dispose pyrolysis flue gas generated in the dangerous waste sludge melting treatment process efficiently and recycle the pyrolysis flue gas, and further, the reduction of the melting treatment cost becomes one of bottleneck factors for popularization and application of an electrothermal melting method.
Disclosure of Invention
The invention aims to solve the technical problems and provide the high-temperature melting pyrolysis flue gas quality-dividing recovery device for hazardous waste sludge, which has the advantages of simple structure, high heat efficiency, cleanness, environmental protection, stability, high efficiency, controllable components, high recovery rate of heavy metal components and capability of realizing continuous production.
The invention discloses a hazardous waste sludge high-temperature melting pyrolysis flue gas quality-classifying recovery device, which comprises a furnace body provided with an induction coil and a crucible arranged in the furnace body, wherein a feed pipe and a primary flue gas collecting hood are arranged at the top of the furnace body, a slag outlet is arranged on the side wall of the furnace body, a slag chute is arranged below the outer side of the slag outlet, and an annular gas collecting hood taking the slag outlet as the center is arranged above the slag chute; the annular gas collecting hood consists of an inner ring gas collecting hood and an outer ring gas collecting hood, wherein the inner ring gas collecting hood is connected with a secondary gas flue, and the outer ring gas collecting hood is connected with a tertiary gas flue.
The feeding pipe penetrates through the primary flue gas collecting hood and stretches into the center of the top of the crucible, and the primary flue gas collecting hood is connected with the primary flue gas pipe.
A baffle plate group is arranged in the crucible, a baffle channel formed between the baffle plate group and the crucible is communicated with the slag outlet, and the slag outlet is positioned at the middle upper section of the crucible; the crucible and the baffle plate group are both nonmetallic electric heating materials.
The baffle plate group comprises a main baffle plate, a central baffle plate and a lower baffle plate, wherein two sides of the main baffle plate are fixed on the side wall of the crucible, the upper end of the main baffle plate is close to the slag outlet and higher than the slag outlet, and the lower end of the main baffle plate downwards extends to the bottom of the crucible and has a distance from the bottom of the crucible; the central flow splitting plate is positioned on the central line of the lower section of the crucible, two sides of the central flow splitting plate are fixed on the side wall of the crucible, the lower end of the central flow splitting plate is spaced from the bottom of the crucible, the main baffle plate is parallel to the central flow splitting plate, and the lower ends of the main baffle plate are at the same height; the lower baffle plate is positioned between the main baffle plate and the central baffle plate, the lower end of the lower baffle plate is fixed at the bottom of the crucible, and the two sides of the lower baffle plate are fixed on the side wall of the crucible.
The middle part of the lower baffle plate is higher than two sides, and is folded in half along the center vertical line by a certain angle to form a herringbone structure in a overlook state.
The lower end of the lower baffle plate is provided with a slag removal guide hole in a folded position.
The baffle plate group also comprises an inclined baffle plate, the upper end of the inclined baffle plate is fixedly connected with the main baffle plate, the lower end of the inclined baffle plate is fixedly connected with the upper end of the central baffle plate, and the two sides of the inclined baffle plate are fixed on the side wall of the crucible.
At least two smoke exhaust holes are formed in the joint part of the upper end part of the inclined baffle plate and the main baffle plate.
The upper end of the main baffle plate is also connected with a hemispherical crown-shaped material separating cover.
At least one smoke exhaust hole is formed in the material separating cover.
The inside of the furnace of the slag outlet is respectively provided with a left side plate, a right side plate and a top plate, the left side plate, the right side plate and the top plate are fixed between the side wall of the crucible and the main baffle plate, an isolation space with an opening at the bottom is formed by surrounding, and the left side plate and the right side plate are made of nonmetallic electric heating materials.
The feeding pipe penetrates through the primary flue gas collecting hood and stretches into the center of the top of the crucible, and the primary flue gas collecting hood is connected with the primary flue gas pipe.
The intermediate frequency induction furnace creatively applies the intermediate frequency induction furnace used in the metallurgical industry to the smelting treatment of hazardous waste sludge, and has the functions of reducing heavy metals, separating from molten slag and the like when the intermediate frequency induction furnace is used for smelting and treating the hazardous waste sludge, but because the hazardous waste sludge has complex components and is limited by energy consumption and cost in the actual production process, the contradiction of high smelting rate of sludge balls in the intermediate frequency induction furnace and the release lag of volatile matters in the sludge, the contradiction of the reduction lag of heavy metals in the sludge and the contradiction of the accumulation lag of reduced heavy metal liquid drops in the molten phase exists, and the contradiction causes that the molten pyrolysis flue gas is difficult to intensively collect and the heavy metal liquid drops in the molten phase are difficult to separate from the slag phase.
In order to solve the problems that the volatile components contained in the hazardous waste sludge are insufficiently volatilized in the melting pyrolysis process and generate smoke dust to pollute the environment when flowing out along with slag, the heavy metals in the hazardous waste sludge molten phase are reduced to simple substance states which are insufficiently discharged along with slag, secondary pollution exists, the gathering length of simple substance state heavy metal liquid drops distributed in the sludge molten slag is greatly separated from the slag phase, the production capacity of a melting furnace is reduced and the like, the production capacity of the melting furnace is reduced due to longer residence time, and the like, the method is improved on the basis of the existing medium-frequency pyrolysis furnace:
except that a primary flue gas collecting hood is arranged at the top of the furnace, an annular gas collecting hood is arranged by taking a fused slag outlet of a flue gas generating source as the center, flue gas with high concentration of pollutant components is collected by an inner annular gas collecting hood and enters a secondary flue gas pipe to be introduced into a secondary combustion chamber, waste heat is utilized after re-incineration, and the enthalpy of combustible components of the flue gas is recovered; the concentration of the smoke pollution components escaping to the periphery of the inner ring gas collecting hood is low, and the smoke pollution components entering the tertiary smoke pipe collected by the outer ring gas collecting hood are led into the environmental smoke dust remover for dust removal and then discharged. When the inner ring gas collecting hood with smaller exhaust gas quantity of the molten slag outlet pipe can collect all the exhaust gas, the dust removing fan connected with the tertiary gas pipe can be shut down, and the operation cost is saved. The flue gas volume collected by the inner ring gas collecting hood is set according to the combustion air volume required by the secondary combustion chamber and is regulated and controlled by the secondary flue gas fan.
The baffle plate group is arranged in the crucible, and the crucible and the baffle plate group are both made of nonmetallic electric heating materials, so that electromagnetic induction heating, such as silicon carbide ceramic materials, can be realized. The electromagnetic induction heating component contained in the sludge balls is heated under the action of medium frequency induction current, and meanwhile, the crucible made of the nonmetallic electric heating material and the components in the crucible are heated up and heated up rapidly under the action of medium frequency induction current, so that the sludge can be heated up and heated up rapidly besides the reinforced separation of heavy metals in the molten slag phase. The baffle plate group comprises a main baffle plate, a central baffle plate and a lower baffle plate, and the furnace is divided into a preheating zone, a reflow zone, a melting zone, a separation zone and a slag discharging zone in sequence by combining the baffle plate group and the flow direction of the molten phase; the sludge balls put into the furnace by the feed pipe are heated and melted under the heating action of pyrolysis gas, a crucible and a baffle plate, enter a soft melting area and a melting area from a preheating area, enter a separation area through a central baffle plate, fully expose heavy metal liquid drops in a molten slag phase through multiple baffling of the central baffle plate, a lower baffle plate and a main baffle plate, create multiple passes through a heavy metal liquid phase layer deposited at the bottom of the furnace for the molten slag phase through multiple baffling, and improve the absorption probability of the exposed heavy metal liquid drops by the heavy metal liquid phase layer under the action of surface tension.
Furthermore, the middle part of the lower baffle plate is higher than two sides, and is folded in half along the center vertical line by a certain angle to form a herringbone structure in a overlook state. The adoption of the structure with the high middle and the low two ends is beneficial to homogenizing the residence time of the molten liquid phase in the furnace and separating volatile matters and heavy metal droplets in the molten liquid phase from the molten liquid phase. Because the distance from the molten liquid in the central area of the crucible to the molten slag outlet pipe is shorter than the distance from the molten liquid in the peripheral area of the crucible to the molten slag outlet pipe when the molten liquid enters the area between the central baffle and the lower baffle through the gap below the central baffle, the time for the molten liquid in the central area of the crucible to flow out through the molten slag outlet is shorter, and the time for the molten liquid in the peripheral area of the crucible to flow out through the molten slag outlet is longer, thereby leading to dead angles in the flow of the molten liquid in the furnace, reducing the effective utilization rate of the crucible, being unfavorable for the effective escape of volatile components in the molten liquid phase and being unfavorable for the separation of heavy metal droplets in the molten liquid phase. The lower baffle plate is arranged to be high in the middle and low in the two ends, and is folded in half along the center vertical line to form a herringbone structure in a overlook state, so that molten liquid in the area near the periphery of the crucible flows into a melting area between the main baffle plate and the molten slag outlet relatively quickly, and the uniformity of the flow of the molten liquid in the crucible is improved. Meanwhile, the design of the crucible is in a V shape, so that the molten liquid in the area near the periphery of the crucible is favorably drained to the central area of the crucible, and the molten liquid mixing effect is enhanced.
Further, the lower end of the lower baffle plate is provided with a slag removal guide hole, and the slag removal guide hole has the following technical effects:
(1) Is beneficial to the separation of heavy metal droplets in the sludge melt phase. The slag removal flow guide holes can keep the equal height of the liquid level of the metal liquid phase at the two sides of the lower baffle plate, so that the situation that the initial stage of adding the sludge ball is pressed by the added sludge ball is avoided, the metal liquid phase is pressed into a melting zone between the lower baffle plate and a molten slag outlet and cannot return, when the sludge molten liquid phase passes through a lower edge gap of the central baffle plate, the contact time of the sludge molten liquid phase and the metal liquid phase is shortened, the probability that the metal liquid phase absorbs heavy metal droplets wrapped by the sludge molten liquid phase is reduced, and the separation of the heavy metal droplets in the sludge molten liquid is not facilitated.
(2) Certain reflux is formed in the metal liquid phase, so that the mixing effect of the molten liquid phase in the furnace is improved. After the slag removal flow guide holes are arranged, the metal liquid phase flowing from the upper edge of the lower baffle plate to the melting area between the lower baffle plate and the molten slag outlet flows back to the melting area between the lower baffle plate and the central baffle plate through the slag removal flow guide holes, so that backflow is formed, and the mixing of the molten liquid phase in the furnace is facilitated.
(3) The slag removal guide holes can ensure that residual sludge liquid phase and metal liquid phase can be thoroughly poured out when the pyrolysis furnace is inclined for slag removal.
Further, the inclined baffle plate is arranged, the inclined angle of the inclined baffle plate is preferably 45-60 degrees, and meanwhile, the smoke exhaust holes are formed in the inclined baffle plate, so that volatile components collected below the inclined baffle plate and escaping are timely discharged, the residence time of the sludge molten liquid phase in the crucible caused by the fact that gas occupies an effective space in the crucible is avoided being shortened, and escape of volatile components in the sludge molten liquid phase and reduction and separation of heavy metal droplets in the sludge molten liquid phase are facilitated. In addition, when the melting point temperature of the added sludge balls is higher, because the melting slag is easier to heat compared with solid sludge under the action of electromagnetic induction and skin effect, the melting slag phase below the inclined baffle plate is easier to absorb energy and heat under the same power, and the melting slag phase with higher temperature passes through the smoke exhaust holes of the inclined baffle plate to enter the upper part of the inclined baffle plate, so that the liquid phase quantity in the soft melting region of the dangerous waste sludge balls with higher melting point temperature is increased, and the energy absorption and heat heating of the dangerous waste sludge balls are also facilitated.
Further, a smoke discharging hole of the material separating cover is formed in the upper portion of the material separating cover, volatile components escaping from a molten slag phase entering a slag discharging area are led out, the smoke quantity escaping from a molten slag outlet pipe is reduced, and the operation environment is improved; more effectively, the negative pressure state of the slag discharging area is formed through the smoke discharging holes of the material separating cover, so that the escape of volatile components in the molten slag phase is facilitated, the amount of the volatile components carried out along with the molten slag phase is reduced, and the recycling rate of the volatile components is improved.
The inner side of the furnace of the slag outlet pipe is respectively provided with a left side plate, a right side plate and a top plate, the left side plate, the right side plate and the top plate are fixed between the side wall of the crucible and the main baffle plate, an isolation space with an opening at the bottom is formed by surrounding, and the volatile components escaping from the molten slag phase in the slag discharging area are isolated from entering the channel of the molten slag outlet pipe; when slag is discharged, the molten slag phase enters a molten slag outlet pipe from the bottom opening and is discharged out of the furnace. Meanwhile, the left side plate and the right side plate are all nonmetallic electric heating materials, so that the area can be locally heated, the temperature of a molten slag phase is increased, the viscosity of the molten slag phase is reduced, the sedimentation and separation of residual heavy metal liquid phases are facilitated, and the escape of residual volatile components into a slag discharging area in a negative pressure environment are facilitated. When the molten slag outlet discharges normally, a molten slag phase liquid seal can be formed, and the operation elasticity of the system is improved.
According to the invention, the molten slag outlet is arranged at the upper middle part of the crucible, so that continuous production can be realized, feeding and discharging can be realized, the phase quantity of the molten liquid stored in the crucible is increased, the residence time of the molten liquid in the crucible is prolonged, and the sedimentation and separation of the molten heavy metal liquid drops from the molten slag are facilitated.
Furthermore, the bottom material is added into the intermediate frequency induction furnace before the intermediate frequency induction furnace is started, and the added bottom material amount is required to meet the requirement that the liquid surface formed after the bottom material is melted covers the lowest side of the lower baffle plate, namely the height of the two sides of the lower baffle plate fixed at the side wall end of the crucible, so that the concentration of heavy metal droplets wrapped in dangerous waste sludge slag in a metal liquid phase is facilitated. Because the sludge slag enters the lower part of the inclined baffle plate through the gap at the lower edge of the central baffle plate under the compression of the sludge ball added above the sludge slag, the sludge slag passes through the metal liquid phase layer, and once tiny heavy metal droplets in the slag phase are exposed in the metal liquid, the sludge slag is easily absorbed into the liquid phase main body by the metal liquid phase under the action of surface tension, so that the tiny heavy metal droplets in the slag phase are separated from the slag.
The beneficial effects are that:
1) And the residual energy of the waste heat of the flue gas is effectively recovered, and the discharge amount of the flue gas is reduced. Through setting up annular gas-collecting channel, collect the combustion air as two combustion chambers through inner ring gas-collecting channel to the flue gas that pollution component concentration is high to accomplish and replace the combustion air that originally gets into two combustion chambers, retrieved the enthalpy of combustible component in the flue gas, reduced the outer discharge capacity of flue gas.
2) The recycling rate of volatile components in the hazardous waste sludge is improved. Through the arrangement of the multistage baffle plates, the temperature of the separation zone is increased, and meanwhile, the disturbance degree of the molten slag phase is increased, so that the escape of volatile components in the molten slag phase is facilitated.
3) The system safety and the production control stability are improved. The closed areas are arranged through the left side plate, the right side plate and the like of the smoke isolation, so that the channels between the outside and a smoke system are isolated, and the air is reduced from entering the smoke system; the left side plate and the right side plate of the smoke isolation pipe are immersed below the liquid level of the molten slag phase to form a liquid seal, so that pressure fluctuation of a smoke system is prevented.
4) The heavy metal components in the hazardous waste sludge are effectively recovered, and the recycling of the heavy metal components in the hazardous waste sludge is realized. By arranging the multistage baffle plates and utilizing the advantage of rapid temperature rise of the baffle plates under the action of induced current, the molten slag phase is heated, the temperature of the molten slag phase is increased, the viscosity of the molten slag phase is reduced, and the heavy metal separation effect is improved. Meanwhile, by means of baffling, the probability that molten heavy metal liquid drops in the molten slag phase are exposed to the heavy metal liquid phase at the bottom of the crucible is increased, and then the probability that the molten heavy metal liquid drops are absorbed under the action of surface tension is increased.
5) Increases the resource utilization way of the sludge molten slag. Due to the high-efficiency separation of heavy metal components, the heavy metal content in the slag phase is reduced, the harm of heavy metal is reduced, and the utilization channel of the slag phase is widened.
6) And improves the heat efficiency and the production efficiency of the melting furnace. The heating areas of the reflow zone and the melting zone in the furnace are increased by arranging the baffle plate group, so that the volatile matters in the sludge are accelerated to escape in the reflow zone and the melting zone to preheat the sludge balls upwards, and the virtuous circle that the volatile matters contained in the sludge balls further escape in the reflow zone and the melting zone is formed.
The pyrolysis furnace disclosed by the invention has a simple structure, the recovery efficiency of heavy metal components in sludge reaches more than 80%, continuous production can be realized, the flue gas is recycled according to quality, and the pyrolysis furnace is environment-friendly and has low equipment investment and running cost.
Drawings
FIG. 1 is a schematic view in front half section of a pyrolysis furnace according to the present invention;
FIG. 2 is a cross-sectional view A-A of FIG. 1;
FIG. 3 is a cross-sectional view B-B of FIG. 1;
FIG. 4 is a cross-sectional view of C-C in FIG. 1;
FIG. 5 is a front view of the lower baffle 4.1;
fig. 6 is a top view of the lower baffle 4.1.
Wherein, 1, furnace body; 2. an induction coil; 3. a crucible; 4. a flow disassembly plate group, 4.1 and a lower baffle plate; 4.2, a central baffle; 4.3, inclined baffles; 4.4, a main baffle plate; 5. a sludge ball; 6. a furnace body heat preservation layer; 7. a material separating cover; 8. a smoke vent; 9. a feed pipe; 10. a primary flue pipe; 11. a third smoke pipe; 12. a primary flue gas collecting hood; 13. a secondary flue pipe; 14. an outer ring gas collecting hood; 15. an inner ring gas collecting hood; 16. a slag spraying retaining wall; 17. a slag outlet; 18. a slag chute; 19. a top plate; 20. a left side plate; 21. a right side plate; 22. slag removal diversion holes; 23. a smoke vent; 24. an environmental flue gas dust removal fan; 25. a secondary flue gas fan; 26. and (3) melting the slag phase liquid level.
In FIG. 1, (1) a preheating zone; (2) a reflow zone; (3) a melting zone; (4) a separation zone; (5) a slag discharging area; (6) and an isolation region.
Detailed Description
The pyrolysis furnace is further explained below with reference to the accompanying drawings:
referring to the attached drawings, the pyrolysis furnace comprises a furnace body 1 provided with an induction coil 2 and a crucible 3 arranged inside, wherein a feed pipe 9 and a primary flue gas collecting hood 12 are arranged at the top of the furnace body 1, the feed pipe 9 penetrates through the primary flue gas collecting hood 12 to extend into the center of the top of the crucible 3, and the primary flue gas collecting hood 12 is connected with a primary flue gas pipe 10; the side wall is provided with a slag outlet 17, a baffle plate group 4 is arranged in the crucible 3, a baffle channel formed between the baffle plate group 4 and the crucible 3 is communicated with the slag outlet 17, and preferably, the slag outlet 17 is positioned at the middle upper section of the crucible; the crucible and the baffle plate group are both nonmetallic electric heating materials.
The baffle group 4 comprises a main baffle 4.4, a central baffle 4.2, a lower baffle 4.1 and an inclined baffle 4.3.
The two sides of the main baffle plate 4.4 are fixed on the side wall of the crucible 3, the upper end of the main baffle plate is close to the slag outlet 17 (the distance between the main baffle plate 4.4 and the slag outlet 17 is preferably 100-150 mm) and is higher than the slag outlet 17, and the lower end of the main baffle plate extends to the bottom of the crucible 3 and has a distance (preferably 100-150 mm) from the bottom of the crucible 3; a hemispherical-crown-shaped material separating cover 7 is further connected between the upper end of the main baffle plate 4 and the side wall of the crucible 3, and at least one smoke exhaust hole 8 is formed in the top of the material separating cover 7.
The central flow splitting plate 4.2 is positioned on the central line of the lower section of the crucible 3, two sides of the central flow splitting plate are fixed on the side wall of the crucible 3, and the lower end of the central flow splitting plate is spaced from the bottom of the crucible 3 by a distance (preferably 100-150 mm); the main baffle plate 4.4 is parallel to the central flow splitting plate 4.2, and the lower end is equal in height.
The lower baffle plate 4.1 is positioned between the main baffle plate 4.4 and the central baffle plate 4.2, the lower end of the lower baffle plate is fixed at the bottom of the crucible 3, two sides of the lower baffle plate are fixed on the side wall 3 of the crucible, the middle part of the lower baffle plate 4.1 is higher than two sides (preferably 200-250mm high on two sides), a herringbone structure in a overlooking state is formed by doubling a certain angle along a central vertical line, the top of the herringbone is oriented to the direction of the slag outlet 17, and a slag removal diversion hole 22 is arranged at the doubling position of the lower end of the lower baffle plate 4.1.
The upper end of the inclined baffle plate 4.3 is fixed on the main baffle plate 4.4, the lower end is connected with the upper end of the central baffle plate 4.2, the two sides of the inclined baffle plate are fixed on the side wall of the crucible 3, and the inclined angle is preferably 45-60 degrees. The two sides of the joint end of the upper section of the inclined baffle plate 4.3 and the main baffle plate 4 are provided with smoke exhaust holes 23.
The inside of the furnace of the slag outlet 17 is respectively provided with a left side plate 20, a right side plate 21 and a top plate 19, the left side plate 20, the right side plate 21 and the top plate 19 are fixed between the side wall of the crucible 3 and the main baffle plate 4.4, an isolation space with an opening at the bottom is formed around the periphery of the slag outlet 17, the opening at the bottom is immersed downwards in the slag liquid phase in the furnace, and one side is communicated with the outside of the furnace through the slag outlet 17.
A slag chute 18 is arranged below the outer side of the slag outlet 17, an annular gas collecting hood taking the slag outlet 17 as the center is arranged above the slag chute 18, the annular gas collecting hood consists of an inner ring gas collecting hood 15 and an outer ring gas collecting hood 14, the inner ring gas collecting hood 15 is connected with a secondary combustion chamber through a secondary flue gas pipe 13 and a secondary flue gas fan 25, and the outer ring gas collecting hood 14 is connected with an environmental flue gas dust remover through a tertiary flue gas pipe 11 and an environmental flue gas dust removing fan 24; the outer side of the inner ring gas-collecting hood 15 is also provided with a slag-spraying retaining wall 16.
The crucible 3, the baffle plate group 4, the left side plate 20 and the right side plate 21 are all nonmetallic electric heating materials, induction heating can be performed under the condition that the induction coil 2 is electrified, specific materials can be reasonably selected by a person skilled in the art according to operation conditions, such as silicon carbide ceramic materials, and the material separation cover 7 and the top plate 19 are conventional refractory materials.
Method embodiment:
in this embodiment, the hazardous waste sludge is waste water sludge from a steel sheet surface treatment process in the metallurgical industry.
1. Adding a slag forming component and a reducing component into the dangerous waste sludge to prepare a sludge ball 5; the slag forming principle and the reduction process are both the prior art, and a person skilled in the art can reasonably select a proper slag former (such as bauxite), a proper reducing agent (such as pulverized coal or coke powder or other carbon-containing waste) and an appropriate addition amount according to the volatile components and the heavy metal content contained in the sludge by referring to literature, so that the slag forming principle and the reduction process are not particularly limited. In the embodiment, the slag forming component is bauxite, and the addition amount is 5-8% (weight ratio) of the total amount of the sludge balls; the reducing component is coke powder, and the adding amount of the reducing component is 0.5-0.8% (weight ratio) of the total amount of the sludge balls.
2. Adding a bottom material into the furnace, wherein the bottom material is glass slag, metallurgical slag or waste metal and the like after high-temperature melting pyrolysis quenching of sludge without volatile components, and the adding amount is that the liquid level of a liquid phase formed after melting is not lower than the height of two sides of a lower baffle plate 4.1;
3. when the temperature in the furnace is raised to 1300 ℃, a sludge ball is continuously thrown into the furnace through a feed pipe 9, under the skin effect of medium-frequency current, the sludge ball enters a melting zone (3) at the bottom of the furnace from top to bottom through a preheating zone (1) and a reflow zone (2) in sequence, is continuously heated, softened and melted into a molten slag phase, heavy metal components contained in dangerous waste sludge are separated and deposited to the bottom of the furnace through reduction melting and the molten slag phase, pass through a metal liquid phase layer, are absorbed by the metal liquid phase under the action of surface tension, the molten slag sequentially passes through a separation zone (4) between a main baffle plate 4.4 and a central baffle plate 4.2, passes through a slag discharge zone (5) between the main baffle plate 4.4 and the furnace wall, and finally passes through an isolation zone (6) surrounded by a left side plate 20, a right side plate 21 and a top plate 19, is discharged into a slag chute 18 outside the furnace through a slag outlet 17, and flows into a cooling water pool to form glassy slag resource utilization;
wherein volatile matters escaping from the separation zone (4) are discharged into the melting zone (3) through the smoke exhaust holes 23 on the inclined baffle plate 4.3, and volatile matters escaping from the slag discharging zone (5) are discharged into the preheating zone (1) through the smoke exhaust holes 8 on the material separating cover 7.
4. The flue gas in the furnace is upwards collected by the primary flue gas collecting hood 12 and then is discharged by the primary flue gas pipe 10 to enter the secondary combustion chamber for burning; the flue gas escaping from the molten slag phase in the front section of the slag chute 18 is collected by the inner ring gas-collecting hood 15 and then is discharged into the secondary combustion chamber through the secondary flue gas pipe 13, and the flue gas escaping from the molten slag phase in the rear section of the slag chute 18 is collected by the outer ring gas-collecting hood 14 and then is discharged into the environmental smoke dust remover through the tertiary flue gas pipe 11.
5. The secondary flue gas fan 25 is adopted to replace a secondary combustion chamber combustion air fan, and the flue gas collected by the inner ring gas collecting hood 15 is adopted to replace the combustion air of the secondary combustion chamber. The flue gas volume collected by the inner ring gas collecting hood 15 is regulated according to the combustion air volume required by the secondary combustion chamber, and the flue gas escaping from the slag outlet 17 and the slag chute 18 area is firstly collected by the inner ring gas collecting hood 15, and the non-collected part is further collected by the outer ring gas collecting hood 14.
The above process is in a continuous operation state.
Furthermore, the pyrolysis furnace can be provided with a weighing device, heavy metal components brought into the pyrolysis furnace along with the sludge balls are continuously enriched under the absorption of heavy metal liquid phase at the lower part of the crucible 3, the heavy metal liquid phase quantity is continuously increased, the heavy metal liquid phase deposition weight change is induced through the weighing device, when the deposition quantity reaches a set value, the furnace is stopped, part of the heavy metal liquid phase is poured out, and the rest capable of covering the height of the lower baffle plate 4.1 is left.
In the embodiment, compared with the traditional resistance type melting furnace and plasma melting furnace method, the method for treating hazardous waste sludge by adopting the pyrolysis furnace can improve the recovery rate of heavy metals, and the recovery rate is more than 80%.
Claims (12)
1. The hazardous waste sludge high-temperature melting pyrolysis flue gas quality-separating recovery device comprises a furnace body provided with an induction coil and a crucible arranged inside, wherein a feed pipe and a primary flue gas collecting hood are arranged at the top of the furnace body, and a slag outlet is arranged on the side wall of the furnace body; the annular gas collecting hood consists of an inner ring gas collecting hood and an outer ring gas collecting hood, wherein the inner ring gas collecting hood is connected with a secondary gas flue, and the outer ring gas collecting hood is connected with a tertiary gas flue.
2. The hazardous waste sludge high temperature melting pyrolysis flue gas quality recovery device according to claim 1, wherein the feed pipe penetrates through a primary flue gas collecting hood to extend into the center of the top of the crucible, and the primary flue gas collecting hood is connected with a primary flue gas pipe.
3. The hazardous waste sludge high-temperature melting pyrolysis flue gas quality recovery device according to claim 1 or 2, wherein a baffle plate group is arranged in the crucible, a baffle channel formed between the baffle plate group and the crucible is communicated with the slag outlet, and the slag outlet is positioned at the middle upper section of the crucible; the crucible and the baffle plate group are both nonmetallic electric heating materials.
4. The hazardous waste sludge high-temperature melting pyrolysis flue gas quality recovery device according to claim 3, wherein the baffle plate group comprises a main baffle plate, a central baffle plate and a lower baffle plate, wherein two sides of the main baffle plate are fixed on the side wall of the crucible, the upper end of the main baffle plate is close to the slag outlet and higher than the slag outlet, and the lower end of the main baffle plate extends downwards to the bottom of the crucible and has a distance from the bottom of the crucible; the central flow splitting plate is positioned on the central line of the lower section of the crucible, two sides of the central flow splitting plate are fixed on the side wall of the crucible, the lower end of the central flow splitting plate is spaced from the bottom of the crucible, the main baffle plate is parallel to the central flow splitting plate, and the lower ends of the main baffle plate are at the same height; the lower baffle plate is positioned between the main baffle plate and the central baffle plate, the lower end of the lower baffle plate is fixed at the bottom of the crucible, and the two sides of the lower baffle plate are fixed on the side wall of the crucible.
5. The hazardous waste sludge high-temperature melting pyrolysis flue gas quality recovery device according to claim 4, wherein the middle part of the lower baffle plate is higher than the two sides, and is folded in half along the center vertical line by a certain angle to form a herringbone structure in a top view state.
6. The hazardous waste sludge high-temperature melting pyrolysis flue gas quality recovery device according to claim 4 or 5, wherein a slag removal diversion hole is arranged at the lower end doubling position of the lower baffle plate.
7. The hazardous waste sludge high-temperature melting pyrolysis flue gas quality recovery device according to claim 3, wherein the baffle plate group further comprises an inclined baffle plate, the upper end of the inclined baffle plate is fixedly connected with the main baffle plate, the lower end of the inclined baffle plate is fixedly connected with the upper end of the central baffle plate, and the two sides of the inclined baffle plate are fixedly connected with the side wall of the crucible.
8. The hazardous waste sludge high temperature melting pyrolysis flue gas quality recovery device according to claim 7, wherein at least two smoke exhaust holes are formed at the joint of the upper end part of the inclined baffle plate and the main baffle plate.
9. The hazardous waste sludge high-temperature melting pyrolysis flue gas quality recovery device according to claim 4, wherein the upper end of the main baffle plate is also connected with a hemispherical-crown-shaped material separation cover.
10. The hazardous waste sludge high temperature melting pyrolysis flue gas quality recovery device according to claim 9, wherein the material separation cover is provided with at least one smoke exhaust hole.
11. The hazardous waste sludge high-temperature melting pyrolysis flue gas quality-dividing recovery device according to claim 3, wherein the inner side of the furnace of the slag outlet is respectively provided with a left side plate, a right side plate and a top plate, the left side plate, the right side plate and the top plate are fixed between the side wall of the crucible and the main baffle plate, an isolation space with an opening at the bottom is formed by surrounding, and the left side plate and the right side plate are non-metal electric heating materials.
12. The hazardous waste sludge high temperature melting pyrolysis flue gas quality recovery device according to claim 1, wherein the feed pipe penetrates through a primary flue gas collecting hood to extend into the center of the top of the crucible, and the primary flue gas collecting hood is connected with a primary flue gas pipe.
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| CN202310474884.3A CN116678002A (en) | 2023-04-27 | 2023-04-27 | Hazardous waste sludge high-temperature melting pyrolysis flue gas quality-separating recovery device |
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| CN202310474884.3A CN116678002A (en) | 2023-04-27 | 2023-04-27 | Hazardous waste sludge high-temperature melting pyrolysis flue gas quality-separating recovery device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116555571A (en) * | 2023-04-27 | 2023-08-08 | 上海开鸿环保科技有限公司 | Dangerous waste sludge electrothermal melting recycling treatment device |
| CN116555571B (en) * | 2023-04-27 | 2024-05-10 | 上海开鸿环保科技有限公司 | Dangerous waste sludge electrothermal melting recycling treatment device |
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2023
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116555571A (en) * | 2023-04-27 | 2023-08-08 | 上海开鸿环保科技有限公司 | Dangerous waste sludge electrothermal melting recycling treatment device |
| CN116555571B (en) * | 2023-04-27 | 2024-05-10 | 上海开鸿环保科技有限公司 | Dangerous waste sludge electrothermal melting recycling treatment device |
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