Charcoal destructive distillation equipment

Abstract

The invention relates to the technical field of charcoal preparation, in particular to charcoal dry distillation equipment, which comprises a dry distillation cellar body, a main flue, a gas-liquid separator, a combustible gas check valve, a combustible gas recovery pipe and a wood vinegar recovery pipe, a plurality of dry distillation tank bodies are arranged in the dry distillation cellar body, a cover body is arranged at the top of each dry distillation tank body, and a gas outlet is formed in the top of each dry distillation tank body. A water sealing groove is formed in the joint of the dry distillation tank body and the cover body, one end of the main flue is communicated with a gas inlet of the gas-liquid separator, the other end of the main flue penetrates through the cover body and is communicated with the interior of the dry distillation tank body, a gas outlet of the gas-liquid separator is communicated with a gas inlet of the combustible gas check valve through a first auxiliary flue, and a gas outlet of the combustible gas check valve is communicated with a gas outlet of the gas-liquid separator through a second auxiliary flue. A gas outlet of the combustible gas check valve is communicated with the combustible gas recovery pipe through a second auxiliary flue, the bottom of the gas-liquid separator and the bottom of the combustible gas check valve are both communicated with the wood vinegar recovery pipe through collecting pipes, and cooling devices are arranged outside the main flue, the gas-liquid separator and the combustible gas check valve.

Description

Technical Field

[0001] This invention relates to the field of charcoal preparation technology, specifically to a charcoal dry distillation device. Background Technology

[0002] Charcoal is a widely used product in daily life and industrial production. Currently, the main methods for charcoal carbonization include earthen kilns, spontaneous combustion, and dry distillation. While earthen kilns can guarantee charcoal quality, the carbonization time is long, resulting in low production efficiency (generally around 40 days). The carbonization process also produces significant amounts of smoke, with harmful gases in the exhaust being directly released into the atmosphere, severely polluting the environment and failing to meet environmental protection requirements. Most manufacturers use kilns employing the spontaneous combustion method. This method relies on the material itself generating heat to carbonize, essentially an oxygen-deficient combustion process. Its disadvantages include dead zones during carbonization and a low yield. Dry distillation offers a short carbonization time, is smokeless and dust-free, is simple to operate, and guarantees product quality. It achieves a 100% carbonization rate, produces non-crushed charcoal, and has a high appearance quality. Therefore, dry distillation carbonization technology is currently the most suitable for widespread application. However, currently used dry distillation carbonization kilns also have certain shortcomings, mainly low cooling time and efficiency, and the direct release of combustible gases and wood vinegar without separation, impacting the environment and wasting resources. Summary of the Invention

[0003] The purpose of this invention is to provide a charcoal dry distillation device.

[0004] A charcoal dry distillation device includes a dry distillation pit, a main flue, a gas-liquid separator, a combustible gas check valve, a combustible gas recovery pipe, and a wood vinegar recovery pipe. The dry distillation pit contains multiple dry distillation tanks, each with a cover on top. A water-sealing groove is provided at the junction of the tank and the cover. One end of the main flue is connected to the inlet of the gas-liquid separator, and the other end passes through the cover and communicates with the interior of the dry distillation tanks. The outlet of the gas-liquid separator is connected to the inlet of the combustible gas check valve via a secondary flue. The outlet of the combustible gas check valve is connected to the combustible gas recovery pipe via a secondary flue. The bottoms of both the gas-liquid separator and the combustible gas check valve are connected to the wood vinegar recovery pipe via collection pipes. Cooling devices are installed outside the main flue, the gas-liquid separator, and the combustible gas check valve.

[0005] Furthermore, the cooling device includes a water supply pipe, a main flue cooling cylinder, a gas-liquid separator spray pipe, a combustible gas check valve spray pipe, a water receiving tray, and a return water pipe. The main flue cooling cylinder is sleeved outside the main flue. The lower part of the main flue cooling cylinder is connected to the water supply pipe through the main flue cooling cylinder inlet pipe. The upper part of the main flue cooling cylinder is provided with a flue cooling cylinder drain pipe. One end of the gas-liquid separator spray pipe is connected to the water supply pipe, and the other end of the gas-liquid separator spray pipe is located above the gas-liquid separator. One end of the combustible gas check valve spray pipe is connected to the water supply pipe, and the other end of the combustible gas check valve spray pipe is located above the combustible gas check valve. The water receiving tray is located below the flue cooling cylinder drain pipe, the gas-liquid separator, and the combustible gas check valve. The bottom of the water receiving tray is connected to the return water pipe.

[0006] Furthermore, the exterior of the distillation tank is provided with a drain pipe connected to the water seal groove, and a drain valve is provided on the drain pipe.

[0007] Furthermore, the distillation pit body is provided with a heating port that cooperates with the distillation tank body, and the heating port is located at the lower part of the distillation tank body.

[0008] Furthermore, the cover is equipped with a thermometer for detecting the temperature inside the distillation tank.

[0009] Furthermore, the space between the distillation pit and the distillation tank is filled with insulating material.

[0010] Furthermore, a lifting ring is provided at the top of the cover.

[0011] In summary, the present invention has the following beneficial effects:

[0012] This invention separates high-temperature gas containing wood vinegar components using a gas-liquid separator and a combustible gas check valve. The separated wood vinegar is collected through a collection pipe into a wood vinegar recovery pipe, while the combustible gas is collected through a combustible gas recovery pipe, thus eliminating environmental impact. The collected combustible gas and wood vinegar can be reused after recycling, preventing resource waste. The cooling device is used to cool the main flue, gas-liquid separator, and combustible gas check valve, reducing cooling time and improving efficiency. Attached Figure Description

[0013] The present invention will be further described in detail below with reference to the accompanying drawings and specific embodiments:

[0014] Figure 1 This is a three-dimensional structural diagram of the present invention;

[0015] Figure 2 This is the front view of the present invention;

[0016] Figure 3 This is a rear view of the present invention;

[0017] Figure 4 This is a top view of the present invention.

[0018] In the diagram: 1. Dry distillation pit body, 2. Dry distillation tank body, 3. Cover body, 4. Water seal groove, 5. Water discharge pipe, 6. Water discharge valve, 7. Thermometer, 8. Heating port, 9. Lifting ring, 10. Main flue, 11. Gas-liquid separator, 12. Secondary flue 1, 13. Combustible gas check valve, 14. Secondary flue 2, 15. Combustible gas recovery pipe, 16. Collection pipe, 17. Wood vinegar recovery pipe, 18. Water supply pipe, 19. Main flue cooling cylinder, 20. Main flue cooling cylinder inlet pipe, 21. Flue cooling cylinder drain pipe, 22. Gas-liquid separator spray pipe, 23. Combustible gas check valve spray pipe, 24. Water receiving tray, 25. Return water pipe. Detailed Implementation

[0019] To make the objectives, technical solutions, and advantages of the embodiments of the present invention clearer, the technical solutions of the embodiments of the present invention will be clearly and completely described below in conjunction with the embodiments of the present invention. Obviously, the described embodiments are only some embodiments of the present invention, and not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those skilled in the art without creative effort are within the scope of protection of the present invention.

[0020] The following is in conjunction with the appendix Figure 1-4 The present invention will be further described as follows:

[0021] A charcoal dry distillation device includes a dry distillation pit 1, a main flue 10, a gas-liquid separator 11, a combustible gas check valve 13, a combustible gas recovery pipe 15, and a wood vinegar recovery pipe 17. The dry distillation pit 1 contains multiple dry distillation tanks 2 for holding wood. The dry distillation pit 1 has heating ports 8 that cooperate with the dry distillation tanks 2. The heating ports 8 are located at the lower part of the dry distillation tanks 2 and are used to house heating devices, such as gas furnaces, for heating the dry distillation tanks 2. Insulating material is filled between the dry distillation pit 1 and the dry distillation tanks 2 to insulate the dry distillation tanks 2 and prevent heat loss. A cover 3 is provided on the top of the dry distillation tanks 2, and a lifting ring 9 is provided on the top of the cover 3 for easy lifting of the cover 3 to fill with wood and remove charcoal. A thermometer 7 is provided on the cover 3 to detect the internal temperature of the dry distillation tanks 2 during dry distillation.

[0022] A water-sealing groove 4 is provided at the junction of the dry distillation tank 2 and the cover 3. Water placed in the water-sealing groove 4 creates a water seal, preventing air from entering the dry distillation tank 2. A drain pipe 5 connected to the water-sealing groove 4 is provided on the outside of the dry distillation tank 2. A drain valve 6 is installed on the drain pipe 5. After charcoal preparation, opening the drain valve 6 allows the water in the water-sealing groove 4 to be drained. One end of the main flue 10 is connected to the inlet of the gas-liquid separator 11, and the other end of the main flue 10 passes through the cover 3 and connects to the inside of the dry distillation tank 2. The outlet of the gas-liquid separator 11 is connected to the inlet of the combustible gas check valve 13 through the auxiliary flue 12. The outlet of the combustible gas check valve 13 is connected to the combustible gas recovery pipe 15 through the auxiliary flue 14. The bottoms of both the gas-liquid separator 11 and the combustible gas check valve 13 are collected through the collection pipe 16 into the wood vinegar recovery pipe 17. The wood vinegar produced during charcoal dry distillation... The high-temperature gas enters the gas-liquid separator 11 for gas-liquid separation. The separated wood vinegar enters the wood vinegar recovery pipe 17 through the collection pipe 16 for collection. The combustible gas enters the combustible gas check valve 13. The combustible gas contains wood vinegar components, which are cooled by the inner wall of the combustible gas check valve 13, and then enter the wood vinegar recovery pipe 17 through the collection pipe 16 for collection. The combustible gas enters the combustible gas recovery pipe 15 for collection, thus eliminating the impact on the environment. The collected combustible gas and wood vinegar can be reused after recycling, thus preventing resource waste.

[0023] Cooling devices are installed on the outside of the main flue 10, gas-liquid separator 11 and combustible gas check valve 13. The cooling devices are used to cool the main flue 10, gas-liquid separator 11 and combustible gas check valve 13, thereby reducing the cooling time and efficiency. The cooling device includes a water supply pipe 18, a main flue cooling cylinder 19, a gas-liquid separator spray pipe 22, a combustible gas check valve spray pipe 23, a water receiving tray 24, and a return water pipe 25. The main flue cooling cylinder 19 is sleeved outside the main flue 10. The lower part of the main flue cooling cylinder 19 is connected to the water supply pipe 18 through the main flue cooling cylinder inlet pipe 20. The upper part of the main flue cooling cylinder 19 is provided with a flue cooling cylinder drain pipe 21. Cooling water in the water supply pipe 18 enters the main flue cooling cylinder 19 from the main flue cooling cylinder inlet pipe 20 to cool the main flue 10, and then exits from the flue cooling cylinder drain pipe 21. One end of the gas-liquid separator spray pipe 22 is connected to the water supply pipe 18. The other end of the spray pipe 22 is located above the gas-liquid separator 11. The cooling water in the water supply pipe 18 flows through the gas-liquid separator spray pipe 22 to the top of the gas-liquid separator 11 to spray and cool it. One end of the combustible gas check valve spray pipe 23 is connected to the water supply pipe 18, and the other end of the combustible gas check valve spray pipe 23 is located above the combustible gas check valve 13. The cooling water in the water supply pipe 18 flows through the combustible gas check valve spray pipe 23 to the top of the combustible gas check valve 13 to spray and cool it. The water receiving pan 24 is located below the flue cooling cylinder drain pipe 21, the gas-liquid separator 11 and the combustible gas check valve 13. The bottom of the water receiving pan 24 is connected to the return water pipe 25. Water discharged from the flue cooling cylinder drain pipe 21, water cooled by spraying from the gas-liquid separator 11, and water cooled by spraying from the combustible gas check valve 13 flow into the water receiving tray 24 for collection, and then into the return water pipe 25. In this embodiment, the water in the return water pipe 25 can be cooled and then recirculated into the cooling device.

[0024] In summary, this invention is not limited to the specific embodiments described above. Those skilled in the art can make various modifications and alterations without departing from the spirit and scope of this invention. The scope of protection of this invention should be determined by the claims of this invention.

[0025] In the description of this patent, it should be understood that the terms “center,” “upper,” “lower,” “front,” “back,” “left,” “right,” “vertical,” “horizontal,” “top,” “bottom,” “inner,” and “outer,” 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 patent 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 patent.

[0026] In the description of this patent, it should be noted that, unless otherwise explicitly specified and limited, the terms "installation," "connection," "linking," and "setting" should be interpreted broadly. For example, they can refer to a fixed connection or setting, a detachable connection or setting, or an integral connection or setting. Those skilled in the art can understand the specific meaning of the above terms in this patent according to the specific circumstances.

Claims

1. A charcoal dry distillation device, characterized in that, The system includes a dry distillation pit (1), a main flue (10), a gas-liquid separator (11), a combustible gas check valve (13), a combustible gas recovery pipe (15), and a wood vinegar recovery pipe (17). The dry distillation pit (1) contains multiple dry distillation tanks (2). Each dry distillation tank (2) has a cover (3) on its top. A water-sealing groove (4) is provided at the junction of the dry distillation tank (2) and the cover (3). One end of the main flue (10) is connected to the inlet of the gas-liquid separator (11), and the other end of the main flue (10) passes through the cover (3) and connects to the dry distillation tank. The interior of the distillation tank (2) is interconnected. The outlet of the gas-liquid separator (11) is connected to the inlet of the combustible gas check valve (13) through the auxiliary flue (12). The outlet of the combustible gas check valve (13) is connected to the combustible gas recovery pipe (15) through the auxiliary flue (14). The bottoms of the gas-liquid separator (11) and the combustible gas check valve (13) are connected to the wood vinegar recovery pipe (17) through the collection pipe (16). Cooling devices are provided on the outside of the main flue (10), the gas-liquid separator (11) and the combustible gas check valve (13).

2. The charcoal dry distillation equipment as described in claim 1, characterized in that, The cooling device includes a water supply pipe (18), a main flue cooling cylinder (19), a gas-liquid separator spray pipe (22), a combustible gas check valve spray pipe (23), a water receiving tray (24), and a return water pipe (25). The main flue cooling cylinder (19) is sleeved on the outside of the main flue (10). The lower part of the main flue cooling cylinder (19) is connected to the water supply pipe (18) through the main flue cooling cylinder inlet pipe (20). The upper part of the main flue cooling cylinder (19) is provided with a flue cooling cylinder drain pipe (21). The gas-liquid separator spray pipe (22) One end of the gas-liquid separator spray pipe (22) is connected to the water supply pipe (18), and the other end of the gas-liquid separator spray pipe (22) is located above the gas-liquid separator (11). One end of the combustible gas check valve spray pipe (23) is connected to the water supply pipe (18), and the other end of the combustible gas check valve spray pipe (23) is located above the combustible gas check valve (13). The water receiving tray (24) is located below the flue cooling cylinder drain pipe (21), the gas-liquid separator (11) and the combustible gas check valve (13). The bottom of the water receiving tray (24) is connected to the return water pipe (25).

3. The charcoal dry distillation equipment as described in claim 2, characterized in that, The outside of the distillation tank (2) is provided with a drain pipe (5) that is connected to the water seal groove (4), and a drain valve (6) is provided on the drain pipe (5).

4. The charcoal dry distillation equipment as described in claim 3, characterized in that, The dry distillation pit (1) is provided with a heating port (8) that cooperates with the dry distillation tank (2), and the heating port (8) is located at the lower part of the dry distillation tank (2).

5. The charcoal dry distillation equipment as described in claim 4, characterized in that, The cover (3) is equipped with a thermometer (7) for detecting the temperature inside the distillation tank (2).

6. The charcoal dry distillation equipment as described in claim 5, characterized in that, The space between the dry distillation pit (1) and the dry distillation tank (2) is filled with thermal insulation material.

7. The charcoal dry distillation equipment as described in claim 1, characterized in that, The top of the cover (3) is provided with a hanging ring (9).

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