Log batch dry distillation module
By designing a log batch carbonization module and using a combination of hydraulic propulsion and gate valve, continuous carbonization of logs was achieved, solving the problems of low efficiency and environmental protection in traditional carbonization methods, increasing carbonization output and protecting the gate valve structure.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-06-26
- Publication Date
- 2026-03-31
AI Technical Summary
Traditional log carbonization methods have environmental and inefficiency problems, especially the long carbonization cycle and the inability to achieve continuous pyrolysis carbonization.
Design a log batch dry distillation module, including at least two parallel dry distillation tanks and a discharge cooling tank. The continuous feeding and discharging of logs is achieved through the cooperation of a hydraulic propulsion device and a gate valve. Combined with the discharge cooling tank, rapid cooling is performed to achieve flow-through pyrolysis carbonization.
It enables continuous and uninterrupted carbonization of logs, increases carbonization output, and protects the electrical structure of the gate valve by cooling the discharged material, preventing high-temperature damage.
Smart Images

Figure CN224062719U_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The utility model relates to a log dry distillation box technical field, concretely relates to a log batch dry distillation module. BACKGROUND
[0002] The original wood charcoal is a kind of high calorific value charcoal obtained after high-temperature carbonization of discarded fruit wood, branches, tree segments, oak wood, litchi wood, oak wood, bamboo tube, bamboo joint and other raw materials, and the charcoal quality is hard, resistant to burning and long burning time, and the pollutants generated during combustion are less.The traditional production method of original wood charcoal is generally to use earth kiln and brick kiln, but this method has significant environmental problems, and a large amount of smoke will be generated during the carbonization process of the original wood material, and the carbonization period is as long as several days or even half a month.Because of its low efficiency and environmental protection, the traditional earth kiln and brick kiln have been basically eliminated.Industrial production generally uses horizontal carbonization furnace, which can significantly shorten the carbonization period, but usually uses single carbonization process, that is, after the biomass is fed into the carbonization furnace, the furnace is closed for high-temperature smelting, and after carbonization and cooling, the material is discharged, and then the biomass material is supplemented again for the next cycle of carbonization process, which cannot realize continuous and uninterrupted pyrolysis carbonization. SUMMARY
[0003] In order to solve the defects of the above-mentioned technology, the utility model provides a kind of original wood batch dry distillation module that can be carbonized continuously.
[0004] The technical scheme adopted by the utility model to realize the above technical effects is:
[0005] A kind of original wood batch dry distillation module, including at least two parallelly arranged dry distillation boxes and the discharge cooling box connected with the discharge end of the dry distillation box, the dry distillation box is a linear type, the metal heated box body with the same diameter specification in front and back cavities, along the direction of feeding to discharge, it is constituted to have feeding box section, main heated box section and discharge box section, the main heated box section is arranged in high-temperature combustion box chamber, the feeding box section and the discharge box section are arranged outside the high-temperature combustion box chamber, the top of the feeding box section is provided with feeding port and feeding gate valve for opening and closing control of the feeding port, the front end box plate of the feeding box section is provided with hydraulic propulsion device for pushing the material in the feeding box section to fill the main heated box section, the discharge port of the discharge box section is communicated with the discharge cooling box, the discharge cooling box is provided with discharge gate valve for opening and closing control of the discharge port.
[0006] Preferably, in the above-mentioned original wood batch dry distillation module, the discharge cooling box is provided with a heat insulation plate for spacing the space in the box into lower box chamber and upper box chamber, the discharge port of the discharge box section is located below the heat insulation plate, the gate opening of the discharge gate valve is located in the lower box chamber, and the electric drive mechanism of the discharge gate valve is located in the upper box chamber.
[0007] Preferably, in the above-mentioned batch wood pyrolysis module, the heat insulation plate is provided with a gate slot above the position corresponding to the discharge port of the discharge box section, for the up-and-down movement of the gate of the discharge gate valve.
[0008] Preferably, in the above-mentioned batch wood pyrolysis module, the lower box chamber is provided with a butt joint connected with the discharge port of the discharge box section.
[0009] Preferably, in the above-mentioned batch wood pyrolysis module, the discharge gate valve comprises a valve plate seat, a gate, a servo motor, a conical reduction gear box and a lead screw, the inner side of the valve plate seat is provided with a sliding groove, the two sides of the gate are slidingly arranged in the sliding groove, the servo motor is drivingly connected with the lead screw through the conical reduction gear box, and the lower end of the lead screw is drivingly connected with the gate.
[0010] Preferably, in the above-mentioned batch wood pyrolysis module, the upper end of the gate is provided with a bent plate, the bent plate is provided with a lead screw through sleeve hole and a lead screw female sleeve at the position corresponding to the lead screw, and the lower end of the lead screw is threadedly connected with the lead screw female sleeve and passes through the lead screw through sleeve hole.
[0011] Preferably, in the above-mentioned batch wood pyrolysis module, the bottom of the main heat receiving box section is provided with a fixed base, the fixed base is provided with vertically arranged vertical support frames in a single column and in a straight line, the top of the vertical support frames on the adjacent two fixed bases is connected with horizontal cross bars, and the main heat receiving box section is arranged on the horizontal cross bars.
[0012] Preferably, in the above-mentioned batch wood pyrolysis module, the top of the main heat receiving box section is provided with a vertical exhaust pipe, and the left and right sides are provided with horizontal exhaust pipes.
[0013] Preferably, in the above-mentioned batch wood pyrolysis module, the pyrolysis box comprises a metal shell with a hollow filler sandwich and a high-temperature-resistant lining arranged in the hollow filler sandwich.
[0014] The wood batch pyrolysis module has the advantages that the at least two parallel arranged pyrolysis boxes arranged in the high-temperature combustion box chamber can realize batch carbonization of the wood material, the carbonization process is uninterrupted, the pyrolysis box can complete automatic feeding and discharging through the cooperation of the hydraulic propulsion device and the feeding gate valve and the discharging gate valve, the pyrolysis box realizes continuous and uninterrupted flow type pyrolysis carbonization of the wood material, and the carbonization yield of the wood material is greatly improved. In addition, the discharging cooling box arranged at the discharging end can cool the high-temperature finished product carbon after discharging, simultaneously provides cooling protection for the discharging gate valve, and prevents the high temperature at the discharging end from damaging the electrical structure of the gate valve. BRIEF DESCRIPTION OF DRAWINGS
[0015] Figure 1 It is a perspective view of the wood batch pyrolysis module from the feeding end.
[0016] Figure 2 This is a perspective view of the present invention from the discharge end.
[0017] Figure 3 This is a state diagram of the present invention in a high-temperature combustion chamber;
[0018] Figure 4 This is a front view of the present invention at the feed end;
[0019] Figure 5 This is a diagram showing the internal structure of the discharge cooling box described in this utility model;
[0020] Figure 6 This is a cross-sectional view of the discharge cooling box of this utility model at the heat insulation plate.
[0021] Figure 7 This is a perspective view of the discharge gate valve described in this utility model. Detailed Implementation
[0022] To provide a further understanding of this utility model, the following description, with reference to the accompanying drawings and specific embodiments, will further illustrate the present utility model:
[0023] In the description of this utility model, it should be noted that the terms "vertical," "upper," "lower," and "horizontal," etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings. They are used only for the convenience of describing this utility model and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on this utility model. In addition, "first," "second," "third," and "fourth" are used for descriptive purposes only and should not be construed as indicating or implying relative importance.
[0024] In the description of this utility model, it should also be noted that, unless otherwise explicitly specified and limited, the terms "set," "install," "connect," and "link" should be interpreted broadly. For example, they can refer to a fixed connection, a detachable connection, or an integral connection; they can refer to a mechanical connection or an electrical connection; they can refer to a direct connection or a connection through an intermediate medium; and they can refer to the internal communication between two components. Those skilled in the art can understand the specific meaning of the above terms in this utility model according to the specific circumstances.
[0025] Please see Figure 1 , Figure 2 and Figure 3 As shown in the figure, an embodiment of this utility model proposes a log batch dry distillation module, including at least two parallel dry distillation tanks 1 and a discharge cooling tank 4 connected to the discharge end of the dry distillation tanks 1. Specifically, as...Figure 3 As shown, the dry distillation tank 1 is a linear metal heating chamber with identical front and rear cavity diameters. Along the feed-to-discharge direction, it comprises a feed section 11, a main heating section 12, and a discharge section 13. The main heating section 12 is located within the high-temperature combustion chamber 100, while the feed section 11 and discharge section 13 are located outside the high-temperature combustion chamber 100. The high temperature in the high-temperature combustion chamber 100 transfers heat to the dry distillation tank 1, causing high-temperature carbonization of the logs inside, resulting in the finished dry distilled charcoal. Figure 1 and Figure 3 As shown, the top of the feeding box section 11 is equipped with a feeding port and a feeding gate valve 2 for controlling the opening and closing of the feeding port. The front end plate of the feeding box section 11 is equipped with a hydraulic propulsion device 3 for pushing the material in the feeding box section 11 forward to fill the main heating box section 12. The discharge port of the discharge box section 13 is connected to the discharge cooling box 4, and the discharge cooling box 4 is equipped with a discharge gate valve 5 for controlling the opening and closing of the discharge port. When feeding logs, the feeding gate valve 2 is opened, allowing the logs to enter the feeding box section 11 from the feeding port opened at the top of the feeding box section 11. When it is necessary to move the logs towards the rear of the container, the feed gate valve 2 closes, creating a seal at the feed inlet. The hydraulic propulsion device 3 advances the logs in the feed box section 11 forward one stroke and then returns. Then, the feed gate valve 2 is reopened, and logs are fed into the feed inlet. The feed gate valve 2 is then closed, and the hydraulic propulsion device 3 continues to advance the logs in the feed box section 11 forward one stroke. This process is repeated multiple times until the main heating box section 12 is full of logs. After carbonization, the discharge gate valve 5 opens the discharge port of the discharge box section 13. The hydraulic propulsion device 3 advances one stroke, pushing the finished charcoal from the rear of the carbonization box 1 out through the discharge port. Logs are then added from the feed inlet, and the hydraulic propulsion device 3 advances one stroke, gradually pushing all the finished charcoal out of the carbonization box 1. After all the finished charcoal has been pushed out, the carbonization box 1 is simultaneously filled with logs. In the embodiments of this utility model, the two distillation tanks 1 operate in batches. During the carbonization process in one distillation tank 1, the other distillation tank 1 discharges finished charcoal and feeds raw wood. The two distillation tanks 1 operate in a cycle in sequence to realize continuous and uninterrupted flow-type pyrolysis carbonization of raw wood by the distillation tanks.
[0026] Furthermore, in a preferred embodiment of this utility model, such as Figure 5As shown, the discharge cooling box 4 is equipped with a heat insulation plate 41 that divides the internal space into a lower chamber 42 and an upper chamber 43. The discharge port of the discharge box section 13 is located below the heat insulation plate 41, the gate of the discharge gate valve 5 is located in the lower chamber 42, and the electric drive mechanism of the discharge gate valve 5 is located in the upper chamber 43. In a preferred embodiment, the heat insulation plate 41 is made of thick asbestos board for insulation. The lower chamber 42 and the upper chamber 43 are respectively connected to a nitrogen cooling device, which provides low-temperature nitrogen to rapidly cool the lower chamber 42 and the upper chamber 43. The upper chamber 43 protects the electric drive mechanism of the discharge gate valve 5 to prevent damage from the high temperature released after the discharge port is opened. The lower chamber 42 rapidly cools the high-temperature finished charcoal discharged from the discharge port.
[0027] Furthermore, in a preferred embodiment of this utility model, such as Figure 6 As shown, the heat insulation plate 41 is provided with a gate slot 45 above the outlet of the corresponding discharge box section 13, allowing the gate of the discharge gate valve 5 to pass up and down. The outlets of the two distillation tanks 1 are both located in the lower chamber 42 and below the gate slot 45. For easy connection, the lower chamber 42 is provided with a docking part 44 that connects to the outlet of the discharge box section 13.
[0028] Furthermore, in a preferred embodiment of this utility model, such as Figure 7 As shown, the discharge gate valve 5 includes a valve seat 51, a gate 52, a servo motor 53, a bevel gearbox 54, and a lead screw 55. The inner side of the valve seat 51 has a groove 511, and the two sides of the gate 52 are slidably arranged in the groove 511. The servo motor 53 is connected to the lead screw 55 via the bevel gearbox 54, and the lower end of the lead screw 55 is connected to the gate 52. The upper end of the gate 52 has a bending plate 521, which has a lead screw through-hole and a lead screw sleeve 56 at the position corresponding to the lead screw 55. The lower end of the lead screw 55 is threadedly connected to the lead screw sleeve 56 and passes through the lead screw through-hole.
[0029] Furthermore, in a preferred embodiment of this utility model, such as Figure 1 , Figure 2 and Figure 4 As shown, the bottom of the main heating box section 12 is provided with a fixed base 6, and a single row of vertical support frames 7 are arranged in a straight line on the fixed base 6. The tops of the vertical support frames 7 on two adjacent fixed bases 6 are connected to horizontal crossbars 71, and the main heating box section 12 is set on the horizontal crossbars 71. Figure 2 and Figure 4As shown, the top of the main heating box section 12 is equipped with a vertical exhaust pipe 8, and the left and right sides are equipped with horizontal exhaust pipes 81. The cracked gas generated during the high-temperature smoldering and carbonization of the logs is released through the vertical exhaust pipe 8 and the horizontal exhaust pipes 81 into the high-temperature combustion chamber 100 outside the dry distillation box 1, and burns on the outer wall of the main heating box section 12, heating the dry distillation box 1, so that the logs inside the dry distillation box 1 are calcined at high temperature until carbonized, thereby improving the thermal energy utilization rate.
[0030] Furthermore, in a preferred embodiment of this utility model, the distillation tank 1 includes a metal shell with a hollow packing jacket and a high-temperature resistant lining disposed within the hollow packing jacket. The high-temperature resistant lining is composed of ceramic fiber compressed blocks, and the metal shell is made of 253MA high-temperature resistant steel. It should be noted that in embodiments of this utility model, the structure of the feed gate valve 2 is the same as that of the discharge gate valve 5, differing only in their installation positions. Figure 3 As shown, the feed gate valve 2 is installed horizontally, and the discharge gate valve 5 is installed vertically.
[0031] In summary, this invention enables batch carbonization of logs by using at least two parallel-arranged pyrolysis tanks within a high-temperature combustion chamber. The carbonization process is uninterrupted. Through the coordination of a hydraulic propulsion device and inlet and outlet gate valves, the pyrolysis tanks can automatically feed and discharge, achieving continuous, uninterrupted flow-type pyrolysis carbonization of the logs, significantly increasing the carbonization yield. Furthermore, the outlet cooling box at the outlet end cools the high-temperature finished charcoal after discharge and provides cooling protection for the outlet gate valve, preventing damage to its electrical structure from the high temperature at the outlet end.
[0032] The foregoing has shown and described the basic principles, main features, and advantages of this utility model. Those skilled in the art should understand that this utility model is not limited to the above embodiments. The embodiments and descriptions in the specification are merely the principles of this utility model. Various changes and modifications can be made to this utility model without departing from its spirit and scope. All such changes and modifications fall within the scope of protection claimed by this utility model, which is defined by the appended claims and their equivalents.
Claims
1. A log batch retort module, characterized by, The application relates to a pyrolysis box, which comprises at least two parallelly arranged pyrolysis boxes (1) and a discharge cooling box (4) connected with the discharge end of the pyrolysis box (1), the pyrolysis box (1) is a linear metal heat receiving box body with the same diameter of the front and rear cavities, and is provided with a feeding box section (11), a main heat receiving box section (12) and a discharge box section (13) along the feeding-to-discharge direction; the main heat receiving box section (12) is arranged in a high-temperature combustion box chamber (100), the feeding box section (11) and the discharge box section (13) are arranged outside the high-temperature combustion box chamber (100), the top of the feeding box section (11) is provided with a feeding port and a feeding gate valve (2) for opening and closing control of the feeding port, the front end box plate of the feeding box section (11) is provided with a hydraulic propelling device (3) for pushing the material in the feeding box section (11) to fill the main heat receiving box section (12), the discharge port of the discharge box section (13) is communicated with the discharge cooling box (4), and the discharge cooling box (4) is provided with a discharge gate valve (5) for opening and closing control of the discharge port.
2. A log batch retort module according to claim 1, characterised in that, The discharge cooling box (4) is provided with a heat insulation plate (41) for spacing the space in the box into a lower box chamber (42) and an upper box chamber (43), the discharge port of the discharge box section (13) is located below the heat insulation plate (41), the gate opening of the discharge gate valve (5) is located in the lower box chamber (42), and the electric driving mechanism of the discharge gate valve (5) is located in the upper box chamber (43).
3. A log batch retort module according to claim 2, characterised in that, The heat insulation plate (41) is provided with a gate plate slot (45) above the position corresponding to the discharge port of the discharge box section (13) for the up-and-down passing of the gate plate of the discharge gate valve (5).
4. A log batch retort module according to claim 2, characterised in that, The lower box chamber (42) is provided with a butt joint part (44) connected with the discharge port of the discharge box section (13).
5. A log batch retort module according to claim 2, characterised in that, The discharge gate valve (5) comprises a valve plate seat (51), a gate plate (52), a servo motor (53), a conical reduction gear box (54) and a lead screw (55), the inner side of the valve plate seat (51) is provided with a sliding groove (511), the two sides of the gate plate (52) are slidingly arranged in the sliding groove (511), the servo motor (53) is in transmission connection with the lead screw (55) through the conical reduction gear box (54), and the lower end of the lead screw (55) is in transmission connection with the gate plate (52).
6. A log batch retort module according to claim 5, characterised in that, The upper end of the gate plate (52) is provided with a bent plate (521), the bent plate (521) is provided with a lead screw through sleeve hole and a lead screw female sleeve (56) at the position corresponding to the lead screw (55), the lower end of the lead screw (55) is in screw connection with the lead screw female sleeve (56) and passes through the lead screw through sleeve hole.
7. A log batch retort module according to claim 1, characterized in that, The bottom of the main heat receiving box section (12) is provided with a fixed base (6), the fixed base (6) is provided with vertically arranged vertical support frames (7) in a single column and in a straight line, the top of the vertical support frames (7) on the adjacent two fixed bases (6) is connected with horizontal cross bars (71), and the main heat receiving box section (12) is arranged on the horizontal cross bars (71).
8. A log batch retort module according to claim 1, characterized in that, The top of the main heating box section (12) is provided with a vertical exhaust pipe (8), and the left and right sides are provided with a horizontal exhaust pipe (81).
9. A log batch retort module according to claim 1, characterized in that, The dry distillation box (1) comprises a metal shell with a hollow filler interlayer and a high-temperature-resistant lining arranged in the hollow filler interlayer.