A feeding device for continuous low-temperature carbonization of bacterial materials
By designing the feeding device for crushing and grading components and dehumidification output components, the dryness and particle size of bacterial materials are solved, automatic feeding and efficient carbonization are achieved, and energy consumption and cost are reduced.
Patent Information
- Application Number
- CN202510533683.5
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2025-04-27
- Publication Date
- 2025-08-05
- Estimated Expiration
- 2045-04-27
AI Technical Summary
The existing feeding device cannot effectively deal with the dryness and particle size problems of bacterial materials, resulting in high energy consumption, increased cost and poor biochar yield and properties of the carbonization process.
A feeding device including crushing grading components, dehumidification output components and continuous low-temperature carbonization components of bacterial materials is designed. Through drying, crushing, grading and adhesive treatment, the bacterial materials meet the appropriate humidity and particle size requirements, and prevent the humidity of large truffles from meeting the standards and affecting the carbonization efficiency.
It realizes automatic feeding, reduces resource losses, improves carbonization efficiency and the quality of biochar, and saves costs.
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Figure CN120059774B_ABST
Abstract
Description
Technical Field
[0001] The invention relates to the technical field of feeding, and in particular to a feeding device for continuous low-temperature carbonization of fungus materials. Background Art
[0002] Low-temperature carbonization of bacterial feed refers to the process of thermally cracking bacterial feed within a certain temperature range (usually lower than that required for traditional high-temperature carbonization) under controlled oxygen content. This improves the resource utilization of the bacterial feed, reduces environmental pollution, and produces biochar or other carbonized products with specific properties.
[0003] The fungus raw materials required for carbonization need to be kept dry to prevent excessive moisture content from increasing energy consumption and costs during the carbonization process, and may also affect the yield and properties of biochar. At the same time, the physical form of the raw materials (such as particle size, shape, etc.) will also affect the carbonization process and the yield and properties of biochar. In addition, raw materials that are too small will increase fly ash losses during the reaction process or cause side reactions, etc. The existing feeding device cannot effectively handle the fungus raw materials.
[0004] Therefore, it is necessary to provide a feeding device for continuous low-temperature carbonization of fungus material to solve the above problems. Summary of the Invention
[0005] To achieve the above-mentioned object, the present invention provides the following technical solution: a feeding device for continuous low-temperature carbonization of bacterial material, comprising:
[0006] The crushing and grading component is provided with an input port and three output ports, wherein the input port is connected to the bacterial material input component, the small bacterial material mixing conveyor belt and the large bacterial material return conveyor; the three output ports of the crushing and grading component are respectively connected to the dehumidification output component, the large bacterial material return conveyor and the small bacterial material output conveyor belt; the output end of the small bacterial material output conveyor belt is embedded in the small bacterial material mixer, and the upper surface of the small bacterial material mixer is fixedly equipped with a bacterial material adhesive tank;
[0007] The output end of the dehumidification output component is connected to a bacterial material continuous low-temperature carbonization component;
[0008] The crushing and grading assembly comprises:
[0009] A fixed support frame, on which a crushing assembly is fixedly embedded, a crushing driver is provided on one side of the crushing assembly, and the crushing driver is fixedly assembled on the upper surface of the fixed support frame;
[0010] A heating and dehumidifying tank is fixedly mounted directly above the crushing assembly, with an input end and an output end of an air dryer provided inside the tank, and the air dryer is fixedly mounted on the upper surface of the fixed support frame;
[0011] A grading assembly is fixedly mounted on the fixed support frame, and an input end of the grading assembly is arranged directly below the crushing driver;
[0012] A control panel is fixedly assembled on the upper surface of the fixed support frame.
[0013] Preferably, the heating and dehumidifying tank comprises:
[0014] A drying tank is fixedly mounted directly above the crushing assembly. A spiral conveyor belt is fixedly mounted inside the drying tank. The spiral conveyor belt has a main input port on the upper surface of the drying tank and a drop port on the lower surface of the drying tank. The drying tank also has an input and output port for an air dryer.
[0015] The auxiliary input port is fixedly assembled on one side of the main input port.
[0016] Preferably, the upper end of the main input port is fixedly connected to the output end of the large mushroom material reflux conveyor;
[0017] The upper end of the auxiliary input port is provided with a bacterial material input component and an output end of a small bacterial material mixing conveyor belt.
[0018] Preferably, the grading component comprises:
[0019] A fixed bracket, the upper surface of which is inclined, and a rotary driver is fixedly assembled along the inclined direction, wherein the rotary driver has two rotating rings rotatably engaged in the middle portion, and the two rotating rings are perpendicularly arranged to the fixed bracket;
[0020] The small-block bacterial material carrying sleeve is rotatably arranged between the two rotating rings, and the small-block bacterial material carrying sleeve is fixedly assembled on the fixed bracket;
[0021] A uniform fungus material carrying net and a bulk fungus material carrying net are fixedly installed between the two rotating rings;
[0022] The central axes of the small-block fungus material carrying sleeve, the uniform fungus material carrying sleeve net and the large-block fungus material carrying sleeve net coincide with each other and are all parallel to the central line of the inclined surface of the fixing bracket.
[0023] Preferably, a small-block fungus material output port is provided below the end of the small-block fungus material carrying sleeve that is closer to the horizontal plane, and an input end of a small-block fungus material output conveyor belt is provided directly below the small-block fungus material output port.
[0024] Preferably, the surfaces of the uniform fungus material carrying net and the bulk fungus material carrying net are provided with uniform feeding holes, and the aperture of the feeding holes of the bulk fungus material carrying net is larger than the aperture of the feeding holes of the uniform fungus material carrying net.
[0025] Preferably, a uniform bacterial material output port is provided on the side of the uniform bacterial material carrying net that is closer to the horizontal plane, and the uniform bacterial material output port is a double-layer sleeve, the inner layer of the double-layer sleeve is fixed on the side of the large bacterial material carrying net that is closer to the horizontal plane, and the uniform bacterial material output port is fixedly assembled on a fixed bracket, and the input end of the dehumidification output component is provided directly below the uniform bacterial material output port.
[0026] Preferably, the large-block fungus material carrying net is rotatably equipped with a crushed fungus material input port on the side farther from the horizontal plane, and the crushed fungus material input port is fixedly assembled just below the crushing assembly;
[0027] The large mushroom material carrying net is rotatably equipped with a large mushroom material outlet on the side closer to the horizontal plane. The large mushroom material outlet is fixedly embedded in the uniform mushroom material outlet and connected to the input end of the large mushroom material reflux conveyor.
[0028] Preferably, the dehumidification output component includes:
[0029] The secondary dryer has a closed shell fixedly mounted on its input end, and an output belt is horizontally arranged inside the secondary dryer. A fungus material drop port is opened on the closed shell above the input end of the output belt, and the fungus material drop port is arranged directly below the uniform fungus material output port;
[0030] A parameter controller is fixedly mounted on the upper surface of the secondary dryer;
[0031] The bacterial material continuous low-temperature carbonization component is connected to the output end of the output belt.
[0032] Compared with the prior art, the present invention provides a feeding device for continuous low-temperature carbonization of fungus materials, which has the following beneficial effects:
[0033] The present invention can adjust the size of each component according to actual working requirements, so that the device can meet different feeding needs. At the same time, the device can automatically complete the entire feeding work, and while completing the feeding work, it will pre-treat the fungus material to meet the drying requirements, and then crush it and grade the crushed fungus material to obtain fungus material with uniform particle size. A dehumidification output component is provided to further dry the obtained fungus material with uniform particle size to prevent the large fungus material from being crushed during the drying process of the crushing and grading component, and the internal fungus material humidity is not up to standard, thereby affecting the carbonization efficiency and quality. At the same time, the fungus material larger than the set size separated by the crushing and grading component will pass through the large fungus material return conveyor to enter the crushing and grading component again for crushing processing, and the fungus material smaller than the size requirement will be transported to the small fungus material mixer through the small fungus material output conveyor belt, and then the small fungus material mixer will be polymerized with the adhesive added by the fungus material adhesive tank, and then the polymerized fungus material will be transported to the crushing and grading component through the small fungus material mixing conveyor belt for secondary processing, saving costs and reducing resource loss to the greatest extent. BRIEF DESCRIPTION OF THE DRAWINGS
[0034] Figure 1 It is a schematic diagram of the overall structure of the present invention;
[0035] Figure 2 Schematic diagram of the structure of the crushing and grading component of the present invention;
[0036] Figure 3 This is a schematic diagram of the structure of the heating and dehumidification tank in the present invention;
[0037] Figure 4 It is a schematic diagram of the structure of the hierarchical component in the present invention;
[0038] Figure 5 Schematic diagram of the structure of the dehumidification output component of the present invention;
[0039] In the figure: 1. Crushing and grading component; 2. Dehumidification output component; 3. Large bacterium block material return conveyor; 4. Small bacterium block material output conveyor belt; 5. Small bacterium block material mixer; 6. Small bacterium block material mixing conveyor belt; 7. Bacterium material adhesive tank; 11. Fixed support frame; 12. Crushing component; 13. Heating and dehumidifying tank; 14. Grading component; 15. Crushing drive; 16. Control panel; 17. Air dryer; 131. Drying tank; 132. Main input port; 133. Auxiliary input port; 1 34. Spiral conveyor belt; 141. Fixed bracket; 142. Rotating drive; 143. Rotating ring; 144. Small-block fungus material carrying sleeve; 145. Uniform fungus material carrying net; 146. Large-block fungus material carrying net; 147. Small-block fungus material output port; 148. Broken fungus material input port; 149. Large-block fungus material output port; 1410. Uniform fungus material output port; 21. Secondary dryer; 22. Sealing shell; 23. Output belt; 24. Fungus material drop port; 25. Parameter controller. DETAILED DESCRIPTION
[0040] See also Figures 1 to 5 The present invention provides a feeding device for continuous low-temperature carbonization of fungus materials, comprising:
[0041] The crushing and grading component 1 is provided with an input port and three output ports, wherein the input port is connected to the bacterial material input component, the small bacterial material mixing conveyor belt 6 and the large bacterial material return conveyor 3, and the three output ports of the crushing and grading component 1 are respectively connected to the dehumidification output component 2, the large bacterial material return conveyor 3 and the small bacterial material output conveyor belt 4. The output end of the small bacterial material output conveyor belt 4 is embedded in the small bacterial material mixer 5, and the upper surface of the small bacterial material mixer 5 is fixedly equipped with a bacterial material adhesive tank 7;
[0042] The output end of the dehumidification output component 2 is connected to a bacterial material continuous low-temperature carbonization component;
[0043] As a preferred embodiment, the crushing and grading component 1 will first dry the fungus material input by the fungus material input component to make it meet the humidity requirements, and then crush the fungus material. The crushed fungus material will be graded according to the set size. Fungus material larger than the set size will pass through the large-block fungus material return conveyor 3 to enter the crushing and grading component 1 again for crushing. Fungus material that meets the size requirements will be input into the fungus material continuous low-temperature carbonization component through the dehumidification output component 2 for carbonization. The dehumidification output component 2 will further dry the fungus material during the output process to prevent the crushing and grading component 1 from drying large blocks of fungus. After the material is crushed, the humidity of the fungus material inside it does not meet the standard, which in turn affects the carbonization efficiency and quality. The fungus material smaller than the size requirement is transported to the small fungus material mixer 5 through the small fungus material output conveyor belt 4, and then the small fungus material mixer 5 is polymerized with the adhesive added by the fungus material adhesive tank 7, and then the polymerized fungus material is transported to the crushing and grading component 1 through the small fungus material mixing conveyor belt 6 for secondary processing. In actual work, the size requirements of the crushing and grading component 1, the dryness of the dehumidification output component 2 and the type of adhesive in the fungus material adhesive tank 7 should be comprehensively selected according to the actual type of fungus material and carbonization requirements.
[0044] Furthermore, the crushing and grading assembly 1 comprises:
[0045] A fixed support frame 11, on which a crushing assembly 12 is fixedly embedded. A crushing driver 15 is provided on one side of the crushing assembly 12, and the crushing driver 15 is fixedly assembled on the upper surface of the fixed support frame 11;
[0046] The heating and dehumidifying tank 13 is fixedly mounted directly above the crushing assembly 12, and the input and output ends of the air dryer 17 are arranged inside the heating and dehumidifying tank 13, and the air dryer 17 is fixedly mounted on the upper surface of the fixed support frame 11;
[0047] The grading assembly 14 is fixedly mounted on the fixed support frame 11, and the input end of the grading assembly 14 is arranged directly below the crushing driver 15;
[0048] A control panel 16 is fixedly mounted on the upper surface of the fixed support frame 11;
[0049] As a preferred embodiment, the air dryer 17 is in direct contact with the wet bacterial material through a hot drying medium (such as hot air), transfers heat by convection, and takes away the generated steam, thereby achieving a drying effect. The crushing particle size of the crushing component 12 can be adjusted according to actual conditions, and the grading requirements of the grading component 14 should be synchronized with the crushing particle size of the crushing component 12.
[0050] Furthermore, the heating and dehumidifying tank 13 includes:
[0051] A drying tank 131 is fixedly mounted directly above the crushing assembly 12. A spiral conveyor belt 134 is fixedly mounted inside the drying tank 131. The spiral conveyor belt 134 has a main input port 132 formed on the upper surface of the drying tank 131 and a drop port formed on the lower surface of the drying tank 131. The drying tank 131 also has an input and output port for an air dryer 17.
[0052] The auxiliary input port 133 is fixedly mounted on one side of the main input port 132;
[0053] As a preferred embodiment, the drying tank 131 is a cylindrical hollow structure with an input port and an output port at the upper and lower ends, and its material is a heat-insulating material, which can retain heat to the greatest extent while ensuring the entry and exit of the fungus material, thereby preventing heat loss, improving drying efficiency, and reducing drying costs. In addition, the setting of the spiral conveyor belt 134 ensures the accurate transportation of the fungus material while allowing the fungus material to reserve sufficient time in the drying tank 131, thereby ensuring the drying performance of the fungus material to the greatest extent, facilitating the subsequent crushing work, and effectively preventing the occurrence of adhesion.
[0054] Furthermore, the upper end of the main input port 132 is fixedly connected to the output end of the large mushroom material return conveyor 3;
[0055] The upper end of the auxiliary input port 133 is provided with the output end of the bacterial material input component and the small bacterial material mixing conveyor belt 6.
[0056] Furthermore, the grading component 14 includes:
[0057] The upper surface of the fixed bracket 141 is inclined, and a rotation driver 142 is fixedly assembled along the inclined direction. The middle part of the rotation driver 142 is rotatably engaged with two rotation rings 143, and the two rotation rings 143 are perpendicular to the fixed bracket 141;
[0058] The small bacteria block carrying sleeve 144 is rotatably disposed between the two rotating rings 143 and is fixedly assembled on the fixed bracket 141;
[0059] A uniform fungus material carrying net 145 and a bulk fungus material carrying net 146 are fixedly mounted between the two rotating rings 143;
[0060] The central axes of the small-block fungus material carrying sleeve 144, the uniform fungus material carrying sleeve net 145 and the large-block fungus material carrying sleeve net 146 coincide with each other and are all parallel to the central line of the inclined surface of the fixing bracket 141;
[0061] As a preferred embodiment, the rotating driver 142 drives the two rotating rings 143 to rotate, and the two rotating rings 143 drive the uniform fungus material carrying net 145 and the large fungus material carrying net 146 to rotate synchronously, while the small fungus material carrying net 144 always remains stationary.
[0062] Furthermore, a small bacterium material outlet 147 is provided below the end of the small bacterium material carrying sleeve 144 closer to the horizontal plane, and the input end of the small bacterium material output conveyor belt 4 is provided directly below the small bacterium material outlet 147;
[0063] As a preferred embodiment, the fungus material passing through the large-block fungus material carrying net 146 and the uniform fungus material carrying net 145 will fall onto the inner wall of the small-block fungus material carrying sleeve 144, and because the small-block fungus material carrying sleeve 144 is inclined, the small-block fungus material on the inner wall of the small-block fungus material carrying sleeve 144 will slide toward the small-block fungus material output port 147, and fall onto the small-block fungus material output conveyor belt 4 through the small-block fungus material output port 147, and subsequent work will be carried out through the small-block fungus material output conveyor belt 4.
[0064] Furthermore, the surfaces of the uniform fungus material carrying net 145 and the bulk fungus material carrying net 146 are provided with uniform feeding holes, and the aperture of the feeding holes of the bulk fungus material carrying net 146 is larger than the aperture of the feeding holes of the uniform fungus material carrying net 145;
[0065] As a preferred embodiment, the uniform fungus material carrying net 145 and the large fungus material carrying net 146 with different apertures can be adjusted according to actual working conditions, and the aperture of the feed hole of the large fungus material carrying net 146 is always larger than the aperture of the feed hole of the uniform fungus material carrying net 145. The size of the fungus material that meets the requirements should be smaller than the aperture of the feed hole of the large fungus material carrying net 146, and larger than the aperture of the feed hole of the uniform fungus material carrying net 145.
[0066] Furthermore, a uniform bacterial material outlet 1410 is provided on the side of the uniform bacterial material carrying net 145 closer to the horizontal plane. The uniform bacterial material outlet 1410 is a double-layer sleeve, the inner layer of which is fixed to the side of the bulk bacterial material carrying net 146 closer to the horizontal plane. The uniform bacterial material outlet 1410 is fixedly assembled on the fixed bracket 141, and the input end of the dehumidification output component 2 is provided directly below the uniform bacterial material outlet 1410.
[0067] As a preferred embodiment, the fungus material with a smaller aperture than the discharge hole of the large fungus material carrying net 146 passes through the discharge hole of the large fungus material carrying net 146 and falls onto the uniform fungus material carrying net 145; the fungus material with a smaller aperture than the discharge hole of the uniform fungus material carrying net 145 passes through the uniform fungus material carrying net 145 and falls onto the small fungus material carrying sleeve 144; the fungus material that meets the requirements is transported to the dehumidification output component 2 through the uniform fungus material output port 1410. The double-layer sleeve setting of the uniform fungus material output port 1410 can prevent the fungus material that does not meet the requirements from falling into the dehumidification output component 2 and affecting the subsequent carbonization work, and at the same time prevent the fungus material that meets the requirements from falling into other components, causing repeated feeding, thereby affecting the feeding efficiency.
[0068] Furthermore, the large-block fungus material carrying net 146 is rotatably equipped with a crushed fungus material input port 148 on the side farther from the horizontal plane, and the crushed fungus material input port 148 is fixedly assembled just below the crushing assembly 12;
[0069] The large mushroom material carrying net 146 is rotatably mounted on the side closer to the horizontal plane with a large mushroom material outlet 149, which is fixedly embedded in the uniform mushroom material outlet 1410 and connected to the input end of the large mushroom material reflux conveyor 3;
[0070] As a preferred embodiment, the setting of the crushed fungus material input port 148 can enable the crushed fungus material to fall into the bulk fungus material carrying net 146 first. The bulk fungus material carrying net 146 will drop fungus material with a diameter smaller than the discharge hole of the bulk fungus material carrying net 146, and fungus material with a diameter larger than the discharge hole of the bulk fungus material carrying net 146 will fall into the bulk fungus material output port 149. The bulk fungus material output port 149 is embedded in the uniform fungus material output port 1410, and is connected to the bulk fungus material reflux conveyor 3 from the inside of the uniform fungus material output port 1410. The bulk fungus material reflux conveyor 3 penetrates into the bottom of the bulk fungus material output port 149 to transport the fungus material to the crushing and grading component 1.
[0071] Furthermore, the dehumidification output component 2 includes:
[0072] The secondary dryer 21 has a closed shell 22 fixedly mounted on its input end, and an output belt 23 is horizontally arranged inside the secondary dryer 21. A fungus drop port 24 is provided on the closed shell 22 above the input end of the output belt 23. The fungus drop port 24 is located directly below the uniform fungus output port 1410.
[0073] The parameter controller 25 is fixedly mounted on the upper surface of the secondary dryer 21;
[0074] A continuous low-temperature carbonization component for the bacterial material is connected to the output end of the output belt 23;
[0075] As a preferred embodiment, since there may be large pieces of bacterial material in the bacterial material of the input device, after the large pieces of bacterial material enter the crushing and grading component 1, the air dryer 17 only dries the outside of the large pieces of bacterial material, and the bacterial material inside still does not meet the drying requirements. Moreover, after the crushing is completed, it is very likely that there will be bacterial material separated from the large pieces of bacterial material that does not meet the humidity requirements. Therefore, the setting of the secondary dryer 21 can further dry this type of bacterial material to prevent it from affecting the subsequent work. The setting of the closed shell 22 can prevent heat loss to a certain extent, thereby reducing drying costs and saving resources.
[0076] During the specific implementation, the following steps are included: according to the actual type of fungus material and the carbonization requirement, the size requirement of the crushing and grading component 1, the degree of dryness of the dehumidification output component 2 and the type of adhesive of the fungus material adhesive tank 7 are selected; then the crushing and grading component 1 will first dry the fungus material input by the fungus material input component to meet the humidity requirement, and then crush the fungus material. The crushed fungus material will be graded according to the set size. Fungus material larger than the set size will enter the crushing and grading component 1 again through the large fungus material return conveyor 3 for crushing, and fungus material that meets the size requirement will pass through the dehumidification output component 2 is input into the continuous low-temperature carbonization component of the fungus material for carbonization, and the dehumidification output component 2 will further dry the fungus material during the output process to prevent the fungus material moisture inside from failing to meet the standard after the large fungus material is crushed during the drying process of the crushing and grading component 1, thereby affecting the carbonization efficiency and quality. The fungus material smaller than the size requirement is transported to the small fungus material mixer 5 through the small fungus material output conveyor belt 4, and then the small fungus material mixer 5 is polymerized by the adhesive added by the fungus material adhesive tank 7, and then the polymerized fungus material is transported to the crushing and grading component 1 through the small fungus material mixing conveyor belt 6 for secondary processing.
[0077] The above is only a preferred specific embodiment of the present invention, but the scope of protection of the present invention is not limited thereto. Any technician familiar with this technical field, within the technical scope disclosed by the present invention, who makes equivalent replacements or changes based on the technical solutions and inventive concepts of the present invention, should be covered by the scope of protection of the present invention.
Claims
1. A feeding device for continuous low-temperature carbonization of bacterial material, characterized in that: include: The crushing and grading component (1) is provided with an input port and three output ports, wherein the input port is connected to the bacterial material input component, the small bacterial material mixing conveyor belt (6) and the large bacterial material return conveyor (3), and the three output ports of the crushing and grading component (1) are respectively connected to the dehumidification output component (2), the large bacterial material return conveyor (3) and the small bacterial material output conveyor belt (4), the output end of the small bacterial material output conveyor belt (4) is embedded in the small bacterial material mixer (5), and the upper surface of the small bacterial material mixer (5) is fixedly equipped with a bacterial material adhesive tank (7); The output end of the dehumidification output component (2) is connected to a bacterial material continuous low-temperature carbonization component; the crushing and grading component (1) comprises: A fixed support frame (11) is fixedly embedded with a crushing assembly (12), a crushing driver (15) is provided on one side of the crushing assembly (12), and the crushing driver (15) is fixedly assembled on the upper surface of the fixed support frame (11); A heating and dehumidifying tank (13) is fixedly mounted directly above the crushing assembly (12), and an input end and an output end of an air dryer (17) are provided on the inner side of the heating and dehumidifying tank (13), and the air dryer (17) is fixedly mounted on the upper surface of the fixed support frame (11); A grading assembly (14) is fixedly mounted on the fixed support frame (11), and an input end of the grading assembly (14) is arranged directly below the crushing driver (15); A control panel (16) is fixedly mounted on the upper surface of the fixed support frame (11); The grading assembly (14) comprises: The fixed bracket (141) has an upper surface that is inclined and is fixedly equipped with a rotation driver (142) along the inclined surface. The rotation driver (142) has two rotation rings (143) that are rotatably engaged in the middle portion. The two rotation rings (143) are perpendicularly arranged to the fixed bracket (141). A small bacterial material carrying sleeve (144) is rotatably arranged between the two rotating rings (143), and the small bacterial material carrying sleeve (144) is fixedly assembled on the fixed bracket (141); A uniform fungus material carrying net (145) and a bulk fungus material carrying net (146) are fixedly mounted between the two rotating rings (143); The central axes of the small-block fungus material carrying sleeve (144), the uniform fungus material carrying sleeve net (145) and the large-block fungus material carrying sleeve net (146) coincide with each other and are all parallel to the central line of the inclined plane of the fixed bracket (141).
2. A feeding device for continuous low-temperature carbonization of bacterial material according to claim 1, characterized in that: The heating and dehumidifying tank (13) comprises: A drying tank (131) is fixedly mounted just above the crushing assembly (12); a spiral conveyor belt (134) is fixedly mounted inside the drying tank (131); a main input port (132) is provided on the upper surface of the drying tank (131); a drop port is provided on the lower surface of the drying tank (131); and an input end and an output end of an air dryer (17) are provided inside the drying tank (131); The auxiliary input port (133) is fixedly assembled on one side of the main input port (132).
3. A feeding device for continuous low-temperature carbonization of bacterial material according to claim 2, characterized in that: The upper end of the main input port (132) is fixedly connected to the output end of the large truffle material return conveyor (3); The upper end of the auxiliary input port (133) is provided with a bacterial material input component and an output end of a small bacterial material mixing conveyor belt (6).
4. A feeding device for continuous low-temperature carbonization of bacterial material according to claim 1, characterized in that: A small bacterium material output port (147) is provided below the end of the small bacterium material carrying sleeve (144) closer to the horizontal plane, and an input end of a small bacterium material output conveyor belt (4) is provided directly below the small bacterium material output port (147).
5. The feeding device for continuous low-temperature carbonization of bacterial material according to claim 1, characterized in that: The surfaces of the uniform fungus material carrying net (145) and the bulk fungus material carrying net (146) are provided with uniform feeding holes, and the aperture of the feeding hole of the bulk fungus material carrying net (146) is larger than the aperture of the feeding hole of the uniform fungus material carrying net (145).
6. A feeding device for continuous low-temperature carbonization of bacterial material according to claim 5, characterized in that: The uniform bacterial material carrying net (145) is rotated to be provided with a uniform bacterial material output port (1410) on the side closer to the horizontal plane. The uniform bacterial material output port (1410) is a double-layer sleeve, the inner layer of which is fixed to the side of the bulk bacterial material carrying net (146) closer to the horizontal plane. The uniform bacterial material output port (1410) is fixedly assembled on the fixed bracket (141), and the input end of the dehumidification output component (2) is provided directly below the uniform bacterial material output port (1410).
7. A feeding device for continuous low-temperature carbonization of bacterial material according to claim 6, characterized in that: The large-block fungus material carrying net (146) is rotatably mounted on a side farther from the horizontal plane with a crushed fungus material input port (148), and the crushed fungus material input port (148) is fixedly mounted directly below the crushing assembly (12); The bulk fungus material carrying net (146) is rotatably mounted on a side closer to the horizontal plane with a bulk fungus material outlet (149), and the bulk fungus material outlet (149) is fixedly embedded in the uniform fungus material outlet (1410) and connected to the input end of the bulk fungus material reflux conveyor (3).
8. A feeding device for continuous low-temperature carbonization of bacterial material according to claim 7, characterized in that: The dehumidification output component (2) comprises: A secondary dryer (21) is fixedly equipped with a closed shell (22) at its input end, and an output belt (23) is horizontally arranged inside the secondary dryer (21), and a bacterial material drop port (24) is opened on the closed shell (22) above the input end of the output belt (23), and the bacterial material drop port (24) is arranged directly below the uniform bacterial material output port (1410); A parameter controller (25) is fixedly mounted on the upper surface of the secondary dryer (21); The bacterial material continuous low-temperature carbonization component is connected to the output end of the output belt (23).
Citation Information
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