Self-heating low-temperature pyrolysis equipment for organic solid waste

Abstract

The utility model discloses organic solid waste self-heating type low-temperature pyrolysis equipment which comprises a magnetization pyrolysis furnace body, a screen plate is fixedly connected in the magnetization pyrolysis furnace body, an electromagnetic heating ring is fixedly installed in the magnetization pyrolysis furnace body, a combustion chamber is arranged on the top of the screen plate, and a feeding door is installed on the left side of the magnetization pyrolysis furnace body. Waste gas generated in the early stage is started by the backflow piece and conveyed into all the hollow metal pipes through the flow dividing pipe set again to be burnt and consumed quickly and efficiently, waste gas leakage is avoided, after the internal temperature reaches the stable pyrolysis temperature, the backflow piece is closed, the exhaust port of the exhaust barrel is opened, harmless gas is exhausted, and the environment is protected. And carbonized dust at the bottom downwards penetrates through the net plate to fall into the lower part, so that the device has the advantages that the solid garbage is rapidly, efficiently and uniformly heated to the pyrolysis temperature, and harmful waste gas generated at the initial stage is subjected to backflow combustion treatment.

Description

Technical Field

[0001] The utility model relates to the field of low-temperature pyrolysis of organic solid waste, and more specifically, to a self-heating low-temperature pyrolysis device for organic solid waste. Background Art

[0002] Low-temperature magnetized pyrolysis furnace is an energy-saving and environmentally friendly equipment for rapid reduction and harmless treatment of organic waste. Its working principle is: the equipment first generates magnetized wind, i.e. magnetized air, through an energy conversion device, and then uses high-energy magnetized air to dry, carbonize and pyrolyze the organic waste in the equipment. After magnetization, the material is first dried and pyrolyzed, and then the harmful gases generated by pyrolysis and gasification are reduced by reducing the amount of magnetized air entering. In addition, under the condition of lack of oxygen, the organic waste is first carbonized and releases a large amount of heat. Under the condition of high heat, the organic matter is continuously pyrolyzed and finally decomposed into small molecules such as carbon dioxide and water vapor and a small amount of residual ash. The low-temperature magnetized pyrolysis furnace uses magnetized air to make gasification and pyrolysis at a low temperature below 350°C, thereby basically eliminating the generation of dioxins. At the same time, it makes full use of the high heat generated by spontaneous combustion of the material, making the energy consumption of the equipment extremely low, and truly realizing the rapid reduction and harmless treatment of garbage.

[0003] However, in the initial stage of heating, the current low-temperature magnetized pyrolysis furnace will heat the solid waste unevenly, which will evaporate some harmful gases. It is difficult to effectively treat the exhaust gas, which will cause some pollution. Utility Model Content

[0004] In view of the problems existing in the prior art, the purpose of the utility model is to provide a self-heating low-temperature pyrolysis device for organic solid waste.

[0005] To solve the above problems, the utility model adopts the following technical solutions.

[0006] A self-heating low-temperature pyrolysis device for organic solid waste comprises a magnetized pyrolysis furnace body, a mesh plate is fixedly connected to the inside of the magnetized pyrolysis furnace body, an electromagnetic heating ring is fixedly installed inside the magnetized pyrolysis furnace body, the top of the mesh plate is a combustion chamber, a feed door is installed on the left side of the magnetized pyrolysis furnace body, an exhaust pipe is fixedly connected to the top of the magnetized pyrolysis furnace body, a reflux piece is installed between the exhaust pipe and the magnetized pyrolysis furnace body, a shunt pipe group connected and coordinated with the reflux piece is installed inside the mesh plate, and a plurality of hollow metal pipes are installed on the shunt pipe group.

[0007] As a further description of the above technical solution: the reflux component includes a control valve, a reflux pipe and a high-temperature induced draft fan. The control valve is fixedly installed on the top of the exhaust pipe. The control valve is connected and fixed with the high-temperature induced draft fan through the reflux pipe. The high-temperature induced draft fan is fixedly installed on the magnetized pyrolysis furnace body. The output end of the high-temperature induced draft fan is connected and fixed with the right end of the diversion pipe group.

[0008] As a further description of the above technical solution: the left end of the diversion pipe group is divided into three branch pipes, and the hollow metal pipes are distributed on the three branch pipes at equal distances.

[0009] As a further description of the above technical solution: the exhaust pipe is installed with an exhaust valve.

[0010] As a further description of the above technical solution: the bottom of the mesh plate is an ash discharge cavity, and ash discharge doors communicating with the ash discharge cavity are provided at the front and rear of the magnetized pyrolysis furnace body.

[0011] As a further description of the above technical solution: a filter plate is fixedly connected to the top of the magnetized pyrolysis furnace body, and the filter plate is located inside the exhaust pipe.

[0012] Compared with the prior art, the advantages of the present invention are:

[0013] This solution uses a reflux piece in conjunction with a diversion pipe group and a hollow metal tube, thereby achieving the advantages of the device being able to quickly, efficiently and evenly heat solid waste to a pyrolysis temperature and to perform reflux combustion treatment on harmful waste gas generated in the early stage. BRIEF DESCRIPTION OF THE DRAWINGS

[0014] Figure 1 It is a three-dimensional structural schematic diagram of the utility model;

[0015] Figure 2 It is a front view cross-sectional structural schematic diagram of the utility model;

[0016] Figure 3 It is a schematic diagram of the cross-sectional structure of the utility model in a top view;

[0017] Figure 4 It is a partial three-dimensional structural schematic diagram of the utility model.

[0018] Description of the numbers in the figure:

[0019] 1. Magnetized pyrolysis furnace body; 2. Screen plate; 21. Ash discharge chamber; 22. Ash discharge door; 3. Electromagnetic heating ring; 4. Combustion chamber; 5. Feed door; 6. Filter plate; 7. Exhaust pipe; 71. Exhaust valve; 8. Reflux part; 81. Control valve; 82. Reflux pipe; 83. High-temperature induced draft fan; 9. Diversion pipe group; 91. Branch pipe; 10. Hollow metal pipe. DETAILED DESCRIPTION

[0020] The following will clearly and completely describe the technical solutions in the embodiments of the present invention in conjunction with the accompanying drawings in the embodiments of the present invention;

[0021] See also Figures 1 to 4 In the utility model, a self-heating low-temperature pyrolysis device for organic solid waste includes a magnetized pyrolysis furnace body 1, a mesh plate 2 is fixedly connected to the inside of the magnetized pyrolysis furnace body 1, an electromagnetic heating ring 3 is fixedly installed inside the magnetized pyrolysis furnace body 1, the top of the mesh plate 2 is a combustion chamber 4, a feed door 5 is installed on the left side of the magnetized pyrolysis furnace body 1, an exhaust pipe 7 is fixedly connected to the top of the magnetized pyrolysis furnace body 1, a reflux piece 8 is installed between the exhaust pipe 7 and the magnetized pyrolysis furnace body 1, a shunt pipe group 9 connected and coordinated with the reflux piece 8 is installed inside the mesh plate 2, and a plurality of hollow metal pipes 10 are installed on the shunt pipe group 9.

[0022] In the utility model, the magnetized pyrolysis furnace body 1 is used as the main body of the device. When in use, the feed door 5 is first opened to put the organic solid waste into the magnetized pyrolysis furnace body 1, and then the electromagnetic heating ring 3 is started to electromagnetically heat the hollow metal tube 10 on the mesh plate 2. Since the hollow metal tube 10 is evenly distributed inside the combustion chamber 4, the organic solid waste is heated more evenly, and the temperature is quickly and evenly raised to the pyrolysis temperature. At this time, the waste gas generated in the early stage is started by the reflux member 8 and re-transported to the inside of each hollow metal tube 10 through the shunt pipe group 9 for fast and efficient combustion consumption, thereby avoiding waste gas. The gas leaks out, and when the internal temperature reaches the stable pyrolysis temperature, the reflux part 8 is closed and the exhaust port of the exhaust pipe 7 is opened to discharge the harmless gas, and the carbonized dust at the bottom passes through the mesh plate 2 and falls below, thereby realizing the advantages of the device for quickly, efficiently and evenly heating the solid waste to the pyrolysis temperature, and reflux combustion treatment of the harmful exhaust gas generated in the early stage, solving the problem that in the low-temperature magnetized pyrolysis furnace in the prior art, due to the solid waste, the waste is heated unevenly at the initial stage of heating, which will evaporate part of the harmful gas, and it is difficult to effectively treat this part of the discharged gas, which will cause some pollution.

[0023] See also Figure 1 and Figure 2 , wherein: the reflux component 8 includes a control valve 81, a reflux pipe 82 and a high-temperature induced draft fan 83, the control valve 81 is fixedly installed on the top of the exhaust pipe 7, the control valve 81 is connected and fixed with the high-temperature induced draft fan 83 through the reflux pipe 82, the high-temperature induced draft fan 83 is fixedly installed on the magnetized pyrolysis furnace body 1, and the output end of the high-temperature induced draft fan 83 is connected and fixed with the right end of the diversion pipe group 9.

[0024] In the utility model, the connection between the exhaust pipe 7 and the return pipe 82 is opened by the control valve 81, and the high-temperature induced draft fan 83 is started to re-inject the waste gas generated initially into the interior of the hollow metal tube 10 for efficient and rapid combustion and cracking, thereby achieving harmless treatment.

[0025] See also Figure 1 and Figure 2 , wherein: the left end of the diversion pipe group 9 is divided into three branch pipes 91 , and the hollow metal pipes 10 are distributed on the three branch pipes 91 at equal distances.

[0026] In the utility model, the branch pipe 91 is used to realize the flow diversion and the even distribution of the hollow metal pipe 10, so that the heating of the solid waste is more efficient and uniform.

[0027] See also Figure 2 , wherein: the exhaust pipe 7 is equipped with an exhaust valve 71.

[0028] In the utility model, the exhaust control of the exhaust pipe 7 is realized through the exhaust valve 71.

[0029] See also Figure 1 and Figure 2 , wherein: the bottom of the mesh plate 2 is an ash discharge cavity 21 , and ash discharge doors 22 communicating with the ash discharge cavity 21 are provided at the front and rear of the magnetized pyrolysis furnace body 1 .

[0030] In the utility model, the carbonized waste is collected through the ash discharge chamber 21 and the ash is cleaned through the ash discharge door 22, which is convenient for operation.

[0031] See also Figure 2 , wherein: a filter plate 6 is fixedly connected to the top of the magnetized pyrolysis furnace body 1 , and the filter plate 6 is located inside the exhaust pipe 7 .

[0032] In the utility model, the filter plate 6 is used to filter a small amount of floating dust during the waste gas recovery and exhaust process to avoid dust pollution.

[0033] The above is only a preferred specific implementation of the utility model; however, the protection scope of the utility model is not limited thereto. Any technician familiar with the technical field can make equivalent replacements or changes according to the technical solution and improved ideas of the utility model within the technical scope disclosed by the utility model, which should be included in the protection scope of the utility model.

Claims

1. A self-heating low-temperature pyrolysis device for organic solid waste, comprising a magnetized pyrolysis furnace body (1), characterized in that: The magnetized pyrolysis furnace body (1) is fixedly connected to a mesh plate (2) inside, an electromagnetic heating ring (3) is fixedly installed inside, the top of the mesh plate (2) is a combustion chamber (4), a feed door (5) is installed on the left side of the magnetized pyrolysis furnace body (1), an exhaust pipe (7) is fixedly connected to the top of the magnetized pyrolysis furnace body (1), a reflux component (8) is installed between the exhaust pipe (7) and the magnetized pyrolysis furnace body (1), a shunt pipe group (9) connected and coordinated with the reflux component (8) is installed inside the mesh plate (2), and a plurality of hollow metal pipes (10) are installed on the shunt pipe group (9).

2. The self-heating low-temperature pyrolysis equipment for organic solid waste according to claim 1, characterized in that: The return component (8) comprises a control valve (81), a return pipe (82) and a high-temperature induced draft fan (83); the control valve (81) is fixedly mounted on the top of the exhaust pipe (7); the control valve (81) is connected and fixedly mounted to the high-temperature induced draft fan (83) via the return pipe (82); the high-temperature induced draft fan (83) is fixedly mounted on the magnetized pyrolysis furnace body (1); and the output end of the high-temperature induced draft fan (83) is connected and fixedly mounted to the right end of the diversion pipe group (9).

3. The self-heating low-temperature pyrolysis equipment for organic solid waste according to claim 1, characterized in that: The left end of the diversion pipe group (9) is divided into three branch pipes (91), and the hollow metal pipes (10) are distributed on the three branch pipes (91) at equal distances.

4. The self-heating low-temperature pyrolysis equipment for organic solid waste according to claim 1, characterized in that: The exhaust pipe (7) is equipped with an exhaust valve (71).

5. The self-heating low-temperature pyrolysis equipment for organic solid waste according to claim 1, characterized in that: The bottom of the mesh plate (2) is an ash discharge cavity (21), and ash discharge doors (22) communicating with the ash discharge cavity (21) are provided at the front and rear of the magnetized pyrolysis furnace body (1).

6. The self-heating low-temperature pyrolysis equipment for organic solid waste according to claim 1, characterized in that: A filter plate (6) is fixedly connected to the top of the magnetized pyrolysis furnace body (1), and the filter plate (6) is located inside the exhaust pipe (7).

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