TW201917156A - Far infrared ray radiant thermal carbonization equipment capable of using heat and carbides generated during a process as a heating fuel to save energy - Google Patents

Abstract

A far-infrared radiant thermal carbonization equipment of the present invention is a far-infrared radiant thermal carbonization equipment which utilizes the same objects A and B, wherein the radiant heat generated by a material of the far infrared ray in a carbonization container is used to heat and to form an overall far-infrared radiant heat environment in the container, then waste is put into the container to be heated by the infrared ray in a sealed space, and the exterior is heated by a burner to dry, thermally decompose and finally carbonize the waste in the container by the action of the far-infrared radiant heat, further, in order to save energy (fuel), the heat and carbides generated by drying and thermal decomposition are injected into the external burner as a heating fuel through a pipeline for reuse, so that the formed carbonized matters, flue gas, and the likes generated in the container are reburned to remove residual substances.

Description

Far infrared radiation heat carbonization equipment

[0001] The present invention relates to a carbonization device, and more particularly to a far-infrared radiant heat carbonization device that uses far-infrared radiant heat to carbonize and crack waste.

[0002] In the past, waste treatment was mainly based on incinerator equipment, which had a large plant and storage space, high equipment investment and maintenance costs, legally difficult to find and expensive, and easy to cause air pollution during the process. Facing issues such as popular protests.

[Problems to be Solved by the Invention] [0003] In view of the above-mentioned known problems, the present inventor proposes a far-infrared radiant heat carbonization device that can be placed in wastes convenient for general indoor use. The carbonization device uses far-infrared The special structure of radiant heat and carbonization container and circulating water pump provides high-performance carbonization device. [Means for Solving the Problems] [0004] In order to solve the above problems, the present invention provides a device for carbonizing and cracking waste, which is a device for the same individuals A and B of carbonizing and cracking waste using far-infrared radiation heat. It is characterized by heating in the body carbonization container by the radiant heat generated by the far red wire material, so that the body carbonization container forms an overall far-infrared radiant heat, putting waste and the like into the body carbonization container, and heating with infrared rays in a closed space. The outside uses a burner to heat the waste in the container to dry and thermally decompose under the action of the far-infrared radiant heat, and finally saves energy (fuel) and reuses the heat and carbides generated by the drying and thermal decomposition. The heated fuel is injected into the external combustion device of the main body through the passage, and the carbonized materials, smoke, and the like generated in the container are subjected to secondary combustion to burn out the remaining materials. [0005] In the present invention, the entire far-infrared radiant heat is formed in the above-mentioned carbonized container. The container is located in a closed body space. The far-infrared ceramic heating layer is used to heat the carbonized container by an external burner, and the fuel is generated by heating. The heat and far-infrared radiant heat will dry and thermally decompose the waste and other materials put into the carbonization container, and finally carbonize, and then introduce the carbonized substances, smoke, odor, etc. generated by the carbonization container into the external heating device through a duct. Combustion to form secondary combustion to reduce carbonized materials, smoke, etc. generated in the container, to save energy and use the carbonized material (flammable gas) as a fuel to quickly warm up to carbonize the waste in the carbonized container. [0006] In the present invention, the heat generated by the above-mentioned drying and thermal decomposition, carbonized substances, etc. are introduced into a gas buffer section by a controller and injected into an external combustion device as a heating fuel for combustion, forming a secondary combustion to carbonize the carbonization chamber. The carbonized materials, smoke and odor generated are minimized, and the tailing treatment combustion device is used to reburn the remaining material that is not completed in the above secondary combustion. The carbonized materials are completely burned. The gaseous substances generated by the products are used for smoke elimination and deodorization. [0007] In addition, in the present invention, the waste and the like put into the carbonization container, the smoke and the thermally decomposed gaseous matter generated by the heating are introduced into the external thermal burner through a duct as a combustion fuel, so as to reduce the amount of the generated in the container. Carbonized materials, and then use one or two or more water circulation devices (water pumps) to cool the thermally decomposed smoke and gaseous materials so that the gaseous materials containing oil, gas, and water are mixed and stored in the circulating water tank. The oil and gas condensed in the cooling water to form slick oil and float in the device. In the device, an ozone machine (O ³ ) is used to inject ozone to decompose the slick oil and organic substances floating on the water surface. [0008] Furthermore, the present invention includes at least one or more water circulation devices (water pumps), which are used in the device to decompose the cracked oil and gas generated by the waste in the container and include at least one or more high temperature combustion treatments Device and catalytic catalyst smoke and deodorizer are used for smoke and deodorization in the device. [0009] In the present invention, the above-mentioned one or two or more sets of water circulation devices (water pumps) are used to extract smoke and gaseous substances in the body of the carbonization device, so that a negative pressure is formed in the carbonization device to prevent leakage from the body of the device. Smoke and odor. [0010] Moreover, in the present invention, the agitator built in the carbonization container can agitate the waste during the carbonization process to uniformly accelerate the carbonization by heating the carbide, so as to save the carbonization time. [0011] In the present invention, carbonized substances, smoke, and odors generated by the carbonization container are introduced into the external heating device through a duct to be burned to eliminate smoke and deodorization. Finally, a main catalyst containing precious metals and titanium oxide and Smoke and deodorizer formed by the far-infrared layer. [0012] The present invention is further explained as follows: 1. A far-infrared heating material is placed inside the carbonized container for heat treatment, a fuel heater is provided externally, the waste is put into the container, and the far-infrared is heated by external combustion in a closed space. The radiant heat heating method heats the above-mentioned container, and the material evaporated by the carbonized container is guided to the external burner for combustion by the controller to form a secondary combustion. In order to increase the heating value and save fuel for the needs of rapid processing and mass production, the above The special structure of the container stirs and pulverizes the waste in the container to accelerate the carbonization, and the heat and far-infrared radiation heat generated by the above method heat the waste to dry, thermally decompose, and finally achieve the purpose of carbonization. [0013] The heating method using far-infrared radiant heat, thermal radiation is an electromagnetic wave, and the conductive heat T1 ⁴ -T2 ⁴ is directly proportional. In general heating methods, the heat transfer between objects has thermal conduction, and convection depends on the heat transfer medium. The heat is proportional to the temperature difference T1-T2 between the two objects. Far-infrared heating is the direct heating and drying of material by radiant heat. Heating and drying using far-infrared radiation can reduce energy loss on media such as air, and it is easy to match characteristics when heat is received. The so-called heat refers to a molecular point of view. Kinetic energy such as inter-atomic vibration stored in an object can be heated more efficiently if it is irradiated with energy in a band of energy that contributes to the inter-atomic motion of the heated body (ie, the infrared active reference vibration wave). For example, water (H ₂ O) is a three-atom molecule, and its reference vibration number is three, that is, the symmetrical stretching vibration of OH is 3652cm ^-1 (2.7um), the reverse symmetrical stretching vibration is 3756cm ^-1 (2.66um), and the variable angle The vibration is 1595cm (6.27um). Water molecules are light molecules with strong binding force. Its basic absorption band is 2.7um, which is close to effectively absorbing infrared rays. Any object emits infrared rays as long as it is not zero. Infrared radiators are used when heating and drying. It is necessary to form infrared radiation characteristics that can effectively promote the movement between heated atoms. [0014] Generally, heating is performed by convection in which hot air is sent into a drying chamber. Drying heating is performed by heating air into convective heat and transmitting heat to the heated body. If the heated substance generates water vapor and its vapor pressure is high, Even if the temperature is increased, it is not easy to dry. The energy water vapor must be quickly released to the outside, and the heat energy not used for drying is lost. If infrared heating is used, the air to be heated will not be heated unnecessarily, and the substance to be heated is directly heated to evaporate. The water vapor quickly dissipates and is effectively heated. [0015] The present invention utilizes the characteristics of heating the infrared rays by an external burner, and is used in the body for heating and drying methods that form the overall far-infrared radiant heat, directly heating the object to be heated, so that the evaporated water vapor is quickly scattered, and the circulating water helps Extraction accelerates the thermal decomposition efficiency, so that the heated material is quickly carbonized, and the vaporized vapors during thermal decomposition are directly introduced into the external burner for combustion, forming secondary combustion, and then attracted and cooled by the circulating water pump to condense the contained oil and gas Floating stored on the water surface, ozone (O ₃ ) is injected into the water through an ozone machine to decompose floating storage materials. [0016] 2. The far-infrared radiant heat is used to heat the catalytic catalyst, and the smoke generated from the waste is deodorized and deodorized. [0017] The use of a catalytic catalyst can reduce the treatment temperature of the exhaust gas and compare it with the general VOC exhaust gas treatment as follows. The main reactions of carbonization treatment with catalytic catalyst are as follows: VOC + O ² catalyst The comparison of CO ₂ + H ² O with catalytic catalyst heating and catalystless catalyst heating for general VOC is as follows: [0018] 3. An externally installed fuel combustion heater uses external heating to heat the far-red line radiation in a closed space. The container body is made of a carbonization device, and a ceramic heating material is installed inside the container body of the carbonization device to form an internal whole. Infrared radiant heat, the carbides in the container are heated through far-infrared ceramic radiant heat, and the carbides projected in the carbonized container are dried and thermally decomposed. At the same time, the special structure in the container stirs and pulverizes the carbides in the container to accelerate carbonization. [0019] 4. Use a secondary burner to vaporize the vaporized decomposition products and smoke and other vapors generated in the carbonization container, and the vapors are high-calorie hydrocarbons, which are directly introduced into the gas buffer section and then injected into the burner. Combustion, carbonizing the above-mentioned gasification and decomposition materials through high-temperature combustion, minimizing the remaining materials, and at the same time increasing the carbonization of the materials in the carbonization container, and then using the exhaust gas treatment combustion equipment to re-burn the incomplete smoke and carbides after the second combustion to eliminate the smoke Deodorization and deodorization by tail gas treatment equipment containing catalytic catalyst. [0020] 5. The water circulating water pump is used to attract the smoke and vapors generated by the carbides in the body of the carbonization device, so that a negative pressure is formed in the body of the carbonization device to prevent the smoke and odor from leaking out of the device body, while cooling the gas The condensed oil is stored on the water surface, and the ozone oil is injected (O ₃ ) to oxidatively decompose the condensed oil and organic matter floating on the water surface. [0021] 6. The smoke and deodorizer can be divided into secondary combustion and exhaust gas treatment combustion and ozone smoke and deodorizer, and the final catalyst smoke and deodorizer is mainly composed of platinum, palladium and titanium oxide. An oxidant, and ozone is injected to break down the components of harmful substances. [0022] The carbonization equipment of the present invention uses a conveyor belt or a lift to put waste into a crusher. The crushed waste is transported by the conveyor belt. During the transportation process, the waste is removed from the water and air-dried and put into a carbonization container. , Push the revolving door switch to close the carbonization container, the external burner heats and uses the radiant heat generated by the far-infrared ceramic material to heat the carbide in the container. The feature of this carbonization equipment is that it adopts full-automatic PLC control to perform carbonization without overheating. Combustion occurs at high temperatures, and the waste in the carbonization container is dried and thermally decomposed by heating with heat from far-infrared radiation heat and heating by an external fuel burner. The vaporized vapors and vapors are guided to the buffer section through a duct and then injected into an external burner for combustion to form a secondary combustion to eliminate smoke, deodorize, and sterilize the vaporized material. They are washed, floated and stored on the water surface with cooling water. The ozone machine is injected (O ₃ ) to decompose and oxidize, and the remaining gasified material is reburned by the exhaust gas burner. Finally, the catalyst smoke deodorizer will de-smoke, deodorize and decompose its harmful substances, and then discharge it to the atmosphere. The carbonized residue in the carbonization container contains a small amount of carbides, which can be treated as waste after general treatment or placed in general soil. [0023] Furthermore, the method for carbonizing waste by the far-infrared carbonization device of the present invention is described as follows: [0024] Dioxin (dioxin) is the most harmful in air pollution. Dioxin is a compound (such as burning plastic, plastic The bag contains dioxin), which is composed of two oxygen atoms connected to a pair of benzene ring compounds. When the general combustion incineration decomposition method is used, the chlorine atoms in the combustion material will form compounds. The method of the present invention uses far-infrared radiant heating to dry, thermally decompose, evaporate, and carbonize the above-mentioned waste in a sealed state. It is completely different from the general combustion method in principle. When oxygen atoms are not supplied, the oxygen atoms combine to generate dioxin. The amount is much reduced compared to the combustion method. [0025] General business wastes and household wastes are infectious and dangerous, as well as the urgency of processing time. Most of the wastes contain plastics such as polyethylene (Polyethlene) or silicone resins. After the far-infrared radiant carbonization method thermally decomposes it into a low-molecular weight compound, chlorine compounds cannot be combined with it, and since polyethylene is a similar molecular substance, the actual reaction will also be combined into dioxin. [0026] The role of far-infrared HHHH polyethylene structure CCCC HHHH Chemical formula: combination of CC and CH [0027] The CC bond of polyethylene absorbs a specific wavelength in far-infrared radiation, and its CH bond absorbs another of the far-infrared radiation After a specific wavelength, it decomposes into active radicals. When the CC bond and CH bond of polyethylene absorb far-infrared rays, they break down and decompose into low-molecular free radicals and react in water. Because polyethylene free radicals are low-molecular substances, they are free of hydrogen. The radical reaction forms a stable low-molecular substance. The low-molecular CC and CH bonds formed are irradiated with far-infrared rays to form a lower-molecular active substance. It reacts with hydrogen atoms to form an oxidizing gas, which carries a grease gas and is cold-cut into water after washing with water. An ozone generator is used. (O ₃ ) Oxidation treatment of substances and oil and gas floating on the water surface can finally oxidize and reduce all organic matter. [0028] The far-infrared radiation carbonization procedure is as follows: Polyethylene Thermal radiation, far-infrared radiation (Thermal decomposition) low-molecular, organic matter Thermal radiation, far-infrared radiation (thermal decomposition), low molecular weight, organic matter Carbon atom (C) (thermal decomposition, thermal oxidative decomposition, oxidation) Inorganic substances, carbon dioxide gas CO ₂ , H ₂ O [0029] Ozone oxidation reaction mechanism: Ozone is a strong oxidant, which will maintain the molecular form of ozone when dissolved in water or After a series of reaction mechanisms, hydroxyl radicals with higher oxidation capacity are formed. Therefore, whether it is ozone or hydroxide radicals, it can destroy organic matter in water with its strong oxidation ability. Reaction of ozone in water as _{follows: O 3 → O + O 2} , O + H 2 O → 2HO, alkaline medium and then O ₃ may OH ^- reaction, a radical generation rate quickly, i.e., O ₃ + OH ^{- _{→ HO 2 + O - 2,}} , HO O ₃ greater than the oxidation _{O 3 + HO 2 → HO +} 2O 2, 2HO 2 → O 3 + H 2 O generated can organics (RH) reaction: HO + RH → R + H ₂ O R + O ₂ → RO ₂ RO ₂ + RH → ROOH + R ROOH + HO → CO ₂ + H ₂ O + ... Other oxidation products [Inventive effect] [0030] 1. Carbonization container The far-infrared ceramic layer is used inside to be heated by the external heater to form the whole far-infrared radiant heat heating. Therefore, the overall far-infrared radiant heat can be heated, and the business waste or general waste in the carbonization container can obtain a good and uniform heat penetration. The effect is that the carbonized container is hermetically sealed and attracted by the water pump to form a negative pressure so that it does not overheat and burn. Especially when processing business waste, most of the materials are polyethylene or resin. Far-infrared radiation heat can be used for carbonization to promote its stability. Thermal decomposition to shorten processing time to thermal decomposition After the formation of low-molecular compounds, they no longer react to become harmful substances. [0031] 2. The far-infrared ceramic layer is installed on the inner wall of the carbonization container. In addition to the waste, the far-infrared ceramic layer can be used for heating and the carbonization container can be heated by using an external combustion device combustion device. The far-infrared ceramic can be made by external heating. The layer forms far-infrared radiant heat, which can subsidize the heating of far-infrared ceramic heating, which can shorten the processing time and save electricity and fuel costs. The far-infrared ceramic layer is formed in the carbonization container, and there is no risk of carbides adhering to the inner surface. . [0032] 3. The built-in agitator in the container drives the motor to raise the agitator link to 170 degrees via the controller (A / B-1a), then release the controller and rotate the spinner to rotate the waste in the container to make the waste Get soaking to accelerate carbonization, which can save processing time and costs. [0033] 4. The water pump is used to attract the gaseous substances in the container to create a negative pressure inside the container, so there is no risk of leakage of smoke, foul odor, etc. It can also accelerate the carbonization time, and its structure is simple and can be used for a long time. The gaseous substances generated in the water pump suction container are washed and cooled, and the substances containing oil and fat components are floated and stored in the water tank. The ozone machine (O ₃ ) is injected into the ozone to decompose the harmful substances, and the smoke is deodorized. [0034] 5. This device has a high effect due to the multiple methods of the first to fifth smoke and deodorizers, and will not cause pollution.

1 and FIG. 2 are far-infrared radiant heat carbonization equipment of two identical entities A and B of the carbonization device body, the inner and outer walls of which are made of durable metal materials, and the inner and outer shells are filled with lightweight heat-insulating materials. Such as magnetized fiber or calcium silicate, etc., a far-red line ceramic magnetic heating layer (A / B-2d) is formed inside the carbonized container (A / B-1), and the body is sealed by a revolving door (A / B-2), and the body is sealed. The hook of the cover (A / B-2a) moves up and down and then enters the rotating shaft (A / B-2b) by the rotation of the hydraulic cylinder to form an internal closed space A / B-2c) to place waste. The far-infrared ceramic layer (A / B-2d) is placed inside the above-mentioned body. The present invention uses a far-infrared ceramic layer, and its auxiliary fuel burner (A / B-5b) is burned by an external combustion device. Gas or diesel can be used. The burner assists in heating the carbonization container, so that the ceramic layer (A / B-2e) inside the carbonization container generates far-infrared radiant heat, and the internal space (A / B-2c) of the carbonization container forms the entire far-infrared radiant heat. [0037] A plan view and a perspective view of the carbonization container (A / B-1) are shown in FIG. 3. The far-infrared ceramic layer (A / B-2d) is coated on the inner wall of the carbonized container (A / B-1). The revolving door (A / B-2) can be controlled by the hydraulic cylinder through PLC (13) automatic control. Open or close, put waste into the container space (A / B-2c), when the carbonization container door is closed, start the external combustion device to heat the far-infrared layer (A / B-2d) and burn the far-infrared ceramic through the combustion device Heating (A / B-2d) to heat the waste in the container to 400 ° C. In addition, the radiant heat generated by the far-infrared ceramic layer (A / B-2d) is used to heat the waste in the carbonized container, which is promoted by the drying and thermal decomposition steps. Evaporation. The heat effect principle is used to heat the spiral flue through the (A / B-2e) flue port, and the exhaust gas is cooled by the air cooling device (A / B-3a) into the gas buffer (A / B-6). The evaporate is controlled and guided by the controller (A / B-4). Its device is equipped with two identical entities A and B. After the introduction of the automatic replacer connector, the carbonized evaporative material produced by the A or B container is converted to the outside. Combustion in the combustion device. When the A container reaches the set temperature, the carbonized material and heat generated by the A container can be introduced into the B external combustion device for combustion, or directly switched to A or B and injected into the combustion device through the buffer to burn ( A / B-5). Inject the substance evaporated from the carbonization container and the flue gas generated from the flue into the buffer (A / B-6) pipe (A / B-6a). Connect the exhaust channel (7a) to the smoke elimination, deodorizer and exhaust gas treatment. When the temperature in the container reaches 280 degrees, start the agitator (A / B-1a) to agitate the waste in the carbonization container to accelerate the carbonization. When the temperature in the container reaches 300 degrees, start the water sprinkler (A / B-2f) and control the amount of water and Accelerate cracking and oxidation at intervals. The air pressure safety valve (A / B-5c) in the container is set to deflate and alarm when the pressure in the container exceeds the set value of the external combustion device. [0038] The first smoke and deodorizer (A / B-5) uses the vapors generated in the carbonization container to return to the external combustion device for combustion, so that the vapors are reburned to eliminate smoke and deodorization to minimize the remaining substances, The vapors produced in the carbonization container are hydrocarbons with high ignition value and are easy to burn. When used as a combustion fuel, the amount of fuel used can be reduced and the carbonization speed and productivity can be increased. [0039] The second smoke and deodorizer uses the first water pump (7) to attract the carbon compounds in the smoke, and applies the principle of constant suction to attract the power of water droplets to drop the flue gas into the water tank to cool the substances containing oil and fat components. It is stored in the water tank and decomposed by the ozone device (O ₃ ), and is used for deodorizing smoke. [0040] The third smoke and deodorizer uses the second water pump (6) to attract carbon compounds in the flue gas, and applies the constant suction principle to attract the profit of water droplets to the flue gas to cool the cold water (10 ) Provide ice water to float the compounds containing light molecules and short-chain substances in the water tank (9b). The second ozone device (O ₃ ) will dissolve and dissolve the smoke and deodorize. [0041] The fourth exhaust gas combustion device (12) uses the burner (12-a) to remove the above-mentioned smoke and deodorization residual substances and burns the above-mentioned treatment residual substances with the burned substances to eliminate undesirable substances such as smoke and odor, and burns them. The special structure of the device, hot air (S), provides hot oxygen to make the carbide easily burn completely and save fuel. [0042] The function of the fifth smoke and deodorizer (12) is to use a built-in catalytic catalyst (12-e) to chemically and physically decompose the vaporized substance in the container by a heater (12-i). ) Heating and catalyzing, heating the oxidation catalyst (12-e) to 320 ° C to decompose the gaseous matter and smoke into low-molecular-weight gaseous matter, and remove the traces of residual light molecules and odors and discharge them into the atmosphere. [0043] Hereinafter, the first smoke removal and deodorizer (A / B-5) combustion device burner (A / B-5a) will be thermally decomposed, and the vapor generated in the carbonization container will be thermally decomposed. [0044] For example: CmHn + O ₂ catalysts such as plastic PE, PVC, silicone, etc. CO ₂ + H ₂ O (CH ₃ ) ₃ N + O ₂ catalyst CO ₂ + H ₂ O + N ₂ VOC + O ₂ catalyst CO ₂ + H ₂ O OH- self-decomposition ^{_{O 3 + OH - → HO 2}} + O - 2 O 3 + OH - → HO - 2 + O 2 HCO - 3 + HO → CO - 3 + H 2 O NH 3 oxidation of ^{_{NH 3 + 4O 3 → NO -}} 3 + H ₃ O Br- oxidation of ^{_{Br - + O 3 → BrO -}} + O 2 HCO - 3 oxygen radical scavenger ^{_{HCO - 3 + HO → HCO 3}} + OH - CI- oxygen radical scavenger CI ^- + OH → HOCI ^- SO ₂ ^-4 oxygen radical scavenger SOI ^2- ₄ + OH → HSO ^- ₄ + H ₂ O [0045] Second, as described above, the ozone in the second and third smoke elimination and deodorizer (7) The device (O ₃ ) is mainly a redox agent, and the chemical reaction of oxidizing or reducing organic components is as follows. [0046] First, the catalytic catalyst (12-e) and the oxidation catalyst are heated to 320 ° C by a heater (12-i) to completely oxidize and decompose the gaseous substances, and (7 and 9) the ozone device is injected with O _{3 to} decompose and is harmful. The substance reacts chemically as follows. O ₃ Direct Reaction: Pollutants + O ₃ → O ₃ intermediate product or indirectly reflect: + HO → product or contaminant intermediate _{O 3 + H 2 O + hv} H 2 O 2 + hv 2HO O 3 (HO 2 - ) HO-CO + 1 / 2O ₂ catalyst CO ₂ Hydrocarbons + O ₂ catalyst CO + H ₂ OH ₂ + 1/2 O ₂ catalyst H ₂ O NO + H ₂ catalyst 1 / 2N ₂ + H ₂ O Hydrocarbons + NO catalyst N ₂ + H ₂ O + CO ₂ CO + H ₂ O Catalyst CO ₂ + H ₂ 2NO + 2CO Catalyst N ₂ + 2CO ₂ CH ₂ COOH + O ₃ (CO ₂ ) n + (H ₂ O) m H ₂ CCHCl + O ₃ H ₂ O + CO ₂ + Cl Cl + H ₂ O + NaOH NaCl + H ₂ O [0047] The remaining traces of carbides after the carbonization of the waste in the container are discharged into the ash slag storage barrel through the ash discharge device (4) and the ash discharge control valve (4a). The storage quantitative control is controlled by the control valve (4b). The plastic bag or sack is connected to the ash outlet (4e) for filling, and the ash residue is completely carbonized and can be treated as general waste or as soil mixture.

[0048]

A / B‧‧‧Carbonized container

A / B-1‧‧‧‧Carbonization equipment body

A / B-1a‧‧‧Carbonization equipment body stirring device

A / B-1b‧‧‧Carbonized Evaporator Outlet

A / B-1c‧‧‧‧Carbonization equipment body flue exit

A / B-1d‧‧‧Layer

A / B-1e‧‧‧Carbonization equipment body carbonization residue export

A / B-1f‧‧‧‧Carbonized Residue Storage Bucket

A / B-2‧‧‧Carbonized container sealed swing arm

A / B-2a‧‧‧Carbonized container sealed revolving door

A / B-2b‧‧‧Hydraulic Cylinder Tactile Carbonized Container Sealed Rotation Kit

A / B-2c‧‧‧Carbonization container space

A / B-2d‧ far-infrared ceramic heating layer built into the carbonized container

A / B-2e‧‧‧Body of carbonized container flue

A / B-2f‧‧‧Sprinkler

A / B-3‧‧‧ body carbonized container flue channel safety air pressure valve

A / B-3a‧‧‧Carbonization container flue channel air cooling equipment

A / B-3b‧‧‧Fan channel air cooling equipment fan for carbonized container

A / B-3c ‧‧‧ Drain pipe in air cooling device of flue channel of carbonized container

A / B-4‧‧‧Body Carbonization Vessel Evaporator Controller

A / B-4a‧‧‧controller first switch

A / B-4b‧‧‧ Controller 2nd Switch

A / B-5‧‧‧Body external combustion device

A / B-5a‧‧‧Body External Burner

A / B-5b‧‧‧‧Carbonized vaporized buffer

A / B-5c‧‧‧External burner safety valve

A / B-5d‧‧‧External burner inner high temperature tile

A / B-6‧‧‧‧Carbonized Evaporate and Flue Gas Buffer Department

A / B-6a‧‧‧ Connected to water treatment equipment pipeline

7‧‧‧ (Using the siphon principle of the power of water to provide attraction) The first water circulation device

7-a‧‧‧air inlet

7-b‧‧‧Water Treatment Circulation Bucket

7-c‧‧‧Water Treatment Circulation Bucket with Built-in Water Pipe

7-d‧‧‧The first pumping circulation pump (motor)

7-e‧‧‧The first treatment circulating water tank

7-f‧‧‧Ozone machine (O ₃ )

7-g‧‧‧washed exhaust gas discharge channel

7-h‧‧‧Water Level Sensor

8‧‧‧ Water Tower Radiator

9‧‧‧Second water circulation device

9-a‧‧‧Second pumping circulation pump

9-b‧‧‧Second treatment circulating water tank

9-c‧‧‧Ozone machine (O ₃ )

9-d‧‧‧washed exhaust gas discharge channel

9-e‧‧‧ Water Level Sensor

10‧‧‧Ice cold water machine

11‧‧‧Using Siphon Principle

11-a‧‧‧Exhaust gas drop channel

11-b‧‧‧Third pumping circulation pump

11-c‧‧‧Exhaust gas outlet

11-d‧‧‧Water Level Sensor

11-e‧‧‧Third treatment circulating water tank

12‧‧‧ tail gas combustion device

12-a‧‧‧ burner

12-b‧‧‧cooling bucket

12-c‧‧‧Cooling water circulation pump

12-d‧‧‧Water cooling circulation device

12-e‧‧‧precious metal catalyst bed device

12-f‧‧‧Exhaust Fan

12-g‧‧‧Final gas buffer

12-h‧‧‧ chimney exhaust

12-i‧‧‧catalyst bed heater

13‧‧‧PLC automatic control system

[0035] FIG. 1 is a detailed explanatory cross-sectional view of each structure and flow of a specific embodiment of a far-infrared radiant heat carbonization device of the present invention. FIG. 2 shows a cross-sectional view of a specific embodiment of the far-infrared radiant heat carbonization device of the present invention. FIG. 3 is a detailed configuration diagram of the carbonization container of the present invention. FIG. 4 is a structural diagram of a circulating water (pump) pump in a far-infrared radiant heat carbonization device of the present invention. Figure 5 is a structural diagram of a carbonized vapor controller and a buffer produced by two identical carbonized containers of the present invention. Fig. 6 is a structural diagram of a flue gas cooling device in a far-infrared radiant heat carbonization device of the present invention. 7 is a structural diagram of a buffer in a far-infrared radiant heat carbonization device of the present invention. FIG. 8 is a structural diagram of an exhaust gas catalyst device in a far-infrared radiant heat carbonization device of the present invention. FIG. 9 is a flowchart of a far-infrared radiant heat carbonization device of the present invention.

Claims (8)

A device for carbonizing and cracking waste is a device for the same individual A and B of carbonizing and cracking waste using far-infrared radiation heat, and is characterized in that the radiant heat generated by the far red wire material is used for heating in the bulk carbonization container, so that the The far-infrared radiant heat is formed in the body carbonization container, and waste is put into the body carbonization container, which is heated by infrared in a closed space, and the outside is heated by a burner to heat the waste in the container to the far-infrared radiation. Under the action of carbon dioxide, it is dried and thermally decomposed and finally carbonized, and the energy (fuel) is saved. The heat generated by the above-mentioned drying and thermal decomposition is used, and the carbide is injected into the external combustion device of the body as a heating fuel through the channel to the carbonized substances generated in the container , Smoke, and other secondary combustion to burn away the remaining material. The device for carbonizing and decomposing waste as described in the first item of the patent application scope, wherein the overall far-infrared radiation heat is formed in the above-mentioned carbonized container, which is located in the closed body space and is heated by an external burner using a far-infrared ceramic heating layer This carbonization container uses the heat generated by fuel heating and far-infrared radiant heat to dry, thermally decompose waste and the like put into the carbonization container, and finally carbonize the carbonized material, smoke, and odor generated by the carbonization container. It is then introduced into the external heating device through a duct for combustion to form secondary combustion to reduce carbonized substances, smoke and the like generated in the container, to save energy and use the carbonized substances (flammable gases) as fuel to rapidly heat to carbonize. Carbonization of waste in containers. The equipment for cracking carbonized waste as described in the second item of the patent application, wherein the heat generated by the above-mentioned drying and thermal decomposition, carbonized materials, etc. are introduced into a gas buffer section by a controller and injected into an external combustion device as a heating fuel for combustion. To form a secondary combustion to minimize the carbonized substances, smoke, and odor generated by its carbonization, and then use the tail treatment combustion device to re-burn the remaining material that was not completed in the secondary combustion, and completely complete the carbonization. Combustion, the gaseous substances generated by waste and the like are deodorized and deodorized by a catalytic catalyst. For example, the equipment for carbonizing and decomposing waste as described in the first or second aspect of the patent application scope, wherein the waste and other wastes put into the carbonization container are heated and the smoke and thermally decomposed gaseous material are introduced into the above as a combustion fuel through a duct. In the external thermal burner, to reduce the carbonized substances generated in the container, one or two or more water circulation devices (water pumps) are used to cool the thermally decomposed smoke and gaseous substances to contain oil and gas. The gaseous material and water are mixed and stored in the circulating water tank. The oil and gas contained in the cooling water is condensed to form a floating oil, which is stored and floated in the device. In the device, an ozone machine (O ³ ) is used to inject ozone to decompose the floating oil floating on the water surface. organic matters. The equipment for cracking carbonized waste as described in item 3 of the scope of patent application, which includes at least one or more water circulation devices (water pumps) for decomposing cracked oil and gas generated by the waste in the container in the device and The smoke and deodorizer including at least one or more high-temperature combustion processors and catalytic catalysts is used for smoke and deodorization in the device from the smoke generated by the carbonized container waste. For example, the equipment for carbonizing and cracking wastes described in item 2 or 4 of the scope of patent application, wherein the above-mentioned one or two or more water circulation devices (water pumps) are used to extract the smoke and gas in the body of the carbonization device, A negative pressure is formed in the carbonization device to prevent smoke and odor from leaking out of the device body. For example, the equipment for carbonizing and cracking wastes described in the second or fourth aspect of the patent application scope, wherein the agitator with a built-in carbonization container can agitate the waste during the carbonization process to uniformly accelerate the carbonization by heating the carbides to save carbonization time. The apparatus for carbonizing and cracking waste as described in the second item of the scope of the patent application, wherein the carbonized substances, smoke, and odor generated by the carbonization container are introduced into the external heating device through a duct to burn and smoke and deodorize, and finally used Main catalyst containing precious metals and titanium oxide, and smoke and deodorizer formed by far-infrared layer.