Charcoal destructive distillation equipment
By designing a charcoal distillation equipment including a gas-liquid separator and a combustible gas check valve, the existing dry distillation carbonization kiln has solved the problems of long cooling time, low efficiency and waste of resources, and efficient recycling of combustible gas and wood vinegar liquid is achieved, protecting the environment and improving production efficiency.
Patent Information
- Application Number
- CN202421927869.6
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-08-09
- Publication Date
- 2025-06-17
- Estimated Expiration
- 2034-08-09
AI Technical Summary
The existing dry distillation carbonization kilns have problems such as long cooling time, low efficiency, and direct discharge of combustible gases and wood vinegar liquid without separation, which affects the environment and causes waste of resources.
A charcoal distillation equipment is designed, including a dry distillation cellar, main flue, gas-liquid separator, combustible gas check valve, combustible gas recovery pipe and wood vinegar liquid recovery pipe. The high-temperature gas is separated by the gas-liquid separator and combustible gas check valve, collecting and recycling combustible gas and wood vinegar liquid, reducing cooling time and improving efficiency.
It effectively eliminates environmental pollution, realizes the recycling and reuse of combustible gases and wood vinegar liquid, improves the efficiency of equipment and reduces resource waste.
Smart Images

Figure CN222990075U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of charcoal preparation, in particular to a charcoal dry distillation device. Background Art
[0002] Charcoal is a product with a relatively large consumption in people's daily life and industrial production. At present, the main carbonization methods for producing charcoal are earth kilns, self-ignition methods, and dry distillation methods. Although earth kilns can ensure the quality of charcoal, the carbonization time is relatively long, the production efficiency is low, generally about 40 days, and a large amount of smoke is generated during carbonization. The harmful gases contained in the tail gas are directly discharged into the atmosphere, seriously polluting the environment and not meeting the environmental protection requirements. Most manufacturers produce kilns using the self-ignition carbonization kiln; the self-ignition method relies on the material itself to generate heat to carbonize itself, which is essentially oxygen-deficient combustion. The disadvantage is that there are dead corners during carbonization and the finished product rate is low. The dry distillation method has a short carbonization time, is smokeless and dust-free, is easy to operate, and the product quality is guaranteed. The carbonization rate is 100%. The carbonized product is not crushed and has a high appearance quality. Therefore, the dry distillation carbonization technology is currently the most suitable carbonization technology for popularization and application. However, the current dry distillation carbonization kiln also has certain deficiencies, mainly including low cooling time and efficiency, direct discharge of combustible gas and wood vinegar liquid without separation, affecting the environment and causing waste of resources, etc. Content of the Utility Model
[0003] The purpose of the utility model is to provide a charcoal dry distillation device.
[0004] A charcoal dry distillation device includes 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 liquid recovery pipe. A plurality of dry distillation tanks are arranged inside the dry distillation cellar body. A cover body is arranged at the top of the dry distillation tank. A water seal groove is arranged at the joint of the dry distillation tank and the cover body. One end of the main flue is communicated with the air inlet of the gas-liquid separator, and the other end of the main flue penetrates through the cover body and is communicated with the inside of the dry distillation tank. The air outlet of the gas-liquid separator is communicated with the air inlet of the combustible gas check valve through a first auxiliary flue. The air outlet of the combustible gas check valve is communicated with the combustible gas recovery pipe through a second auxiliary flue. The bottoms of the gas-liquid separator and the combustible gas check valve are both communicated with the wood vinegar liquid recovery pipe through a collection pipe. A cooling device is arranged outside the main flue, the gas-liquid separator, and the combustible gas check valve.
[0005] Further, 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 water return 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 a main flue cooling cylinder water 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 water return pipe.
[0006] Further, a water discharge pipe communicating with the water seal groove is provided outside the retorting tank body, and a water discharge valve is provided on the water discharge pipe.
[0007] Further, a heating port matching the retorting tank body is provided on the retorting cellar body, and the heating port is located at the lower part of the retorting tank body.
[0008] Further, a thermometer for detecting the internal temperature of the retorting tank body is provided on the cover body.
[0009] Further, a heat insulating material is filled between the retorting cellar body and the retorting tank body.
[0010] Further, a lifting ring is provided at the top of the cover body.
[0011] In summary, the present utility model has the following beneficial effects:
[0012] The present utility model separates the high-temperature gas containing wood vinegar liquid components through a gas-liquid separator and a combustible gas check valve. The separated wood vinegar liquid enters the wood vinegar liquid recovery pipe through a collection pipe for collection, and the combustible gas enters the combustible gas recovery pipe for collection, eliminating the impact on the environment. The collected combustible gas and wood vinegar liquid can be recycled after recovery, eliminating resource waste; the cooling device is used to cool the main flue, the gas-liquid separator and the combustible gas check valve, reducing the time and improving the efficiency of cooling. BRIEF DESCRIPTION OF THE DRAWINGS
[0013] The following further describes the present utility model in detail with reference to the drawings and specific embodiments:
[0014] Figure 1 is a three-dimensional structural schematic diagram of the present utility model;
[0015] Figure 2 is the front view of the present utility model;
[0016] Figure 3This is the rear view of the present utility model;
[0017] Figure 4 This is the top view of the present utility model.
[0018] In the figure: 1 retorting cellar body, 2 retorting tank body, 3 cover body, 4 water seal groove, 5 water discharge pipeline, 6 water discharge valve, 7 thermometer, 8 heating port, 9 lifting ring, 10 main flue, 11 gas-liquid separator, 12 first secondary flue, 13 combustible gas check valve, 14 second secondary flue, 15 combustible gas recovery pipe, 16 collection pipe, 17 wood vinegar liquid recovery pipe, 18 water supply pipe, 19 main flue cooling cylinder, 20 main flue cooling cylinder water 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. Specific embodiments
[0019] To make the objectives, technical solutions and advantages of the embodiments of the present utility model clearer, the technical solutions in the embodiments of the present utility model will be clearly and completely described below in conjunction with the embodiments of the present utility model. Obviously, the described embodiments are part of the embodiments of the present utility model, rather than all of the embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present utility model.
[0020] The following is a further description of the present utility model in conjunction with the attached Figures 1-4 figures:
[0021] A charcoal retorting device includes a retorting cellar body 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 liquid recovery pipe 17. A plurality of retorting tank bodies 2 for placing wood are arranged in the retorting cellar body 1. A heating port 8 matching the retorting tank body 2 is provided on the retorting cellar body 1. The heating port 8 is located at the lower part of the retorting tank body 2 and is used for placing a heating device, such as a gas furnace, for heating the retorting tank body 2. Heat insulation materials are filled between the retorting cellar body 1 and the retorting tank body 2 to keep the retorting tank body 2 warm and prevent heat loss. A cover body 3 is arranged at the top of the retorting tank body 2. A lifting ring 9 is arranged at the top of the cover body 3 to facilitate lifting the cover body 3 for filling wood and taking out charcoal. A thermometer 7 for detecting the temperature inside the retorting tank body 2 is arranged on the cover body 3 to detect the temperature during retorting inside the retorting tank body 2.
[0022] A water seal groove 4 is provided at the joint of the retorting tank body 2 and the cover body 3. After water is placed in the water seal groove 4, it can achieve the effect of water sealing to prevent air from entering the retorting tank body 2. A water discharge pipe 5 communicating with the water seal groove 4 is provided outside the retorting tank body 2, and a water discharge valve 6 is provided on the water discharge pipe 5. After the charcoal preparation is completed, opening the water discharge valve 6 can discharge the water in the water seal groove 4. One end of the main flue 10 is communicated with the air inlet of the gas-liquid separator 11, the other end of the main flue 10 penetrates through the cover body 3 and is communicated with the inside of the retorting tank body 2. The air outlet of the gas-liquid separator 11 is communicated with the air inlet of the combustible gas check valve 13 through the first secondary flue 12, and the air outlet of the combustible gas check valve 13 is communicated with the combustible gas recovery pipe 15 through the second secondary flue 14. The bottoms of the gas-liquid separator 11 and the combustible gas check valve 13 both enter the wood vinegar liquid recovery pipe 17 through the collection pipe 16 for collection; the high-temperature gas containing wood vinegar liquid components generated during charcoal retorting enters the gas-liquid separator 11 for gas-liquid separation. The separated wood vinegar liquid enters the wood vinegar liquid recovery pipe 17 through the collection pipe 16 for collection, and the combustible gas enters the combustible gas check valve 13. The combustible gas containing wood vinegar liquid components cools when it encounters the inner wall of the combustible gas check valve 13 and enters the wood vinegar liquid recovery pipe 17 through the collection pipe 16 for collection; the combustible gas enters the combustible gas recovery pipe 15 for collection, eliminating the impact on the environment. The collected combustible gas and wood vinegar liquid can be recycled after recovery, eliminating resource waste.
[0023] A cooling device is provided outside the main flue 10, the gas-liquid separator 11 and the combustible gas check valve 13. The cooling device is used to cool the main flue 10, the gas-liquid separator 11 and the combustible gas check valve 13, reducing the time and efficiency of cold shortage. 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 water return 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 water inlet pipe 20. A flue cooling cylinder drain pipe 21 is arranged at the upper part of the main flue cooling cylinder 19. The cooling water in the water supply pipe 18 enters the main flue cooling cylinder 19 through the main flue cooling cylinder water inlet pipe 20 to cool the main flue 10, and then is discharged 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, and the other end of the gas-liquid separator 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 upper part of the gas-liquid separator 11 to spray and cool 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 cooling water in the water supply pipe 18 flows through the combustible gas check valve spray pipe 23 to the upper part of the combustible gas check valve 13 to spray and cool 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 water return pipe 25. The water discharged from the flue cooling cylinder drain pipe 21, the water after spraying and cooling the gas-liquid separator 11 and the water after spraying and cooling the combustible gas check valve 13 flow into the water receiving tray 24 for collection, and then flow into the water return pipe 25. In this embodiment, the water in the water return pipe 25 can continue to enter the cooling device for recycling after being cooled.
[0024] In summary, the present utility model is not limited to the above specific embodiments. Those skilled in the art can make several changes and modifications on the premise of not departing from the spirit and scope of the present utility model. The protection scope of the present utility model shall be subject to the claims of the present utility model.
[0025] In the description of this patent, it should be understood that the orientation or positional relationship indicated by the terms "center", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", etc. is based on the orientation or positional relationship shown in the drawings. It is only for the convenience of describing this patent and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore should not be construed as a limitation of this patent.
[0026] In the description of this patent, it should be noted that unless otherwise clearly specified and defined, the terms "installation", "connection", "linkage", and "setting" should be understood in a broad sense. For example, it can be fixedly connected or set, or detachably connected or set, or integrally connected or set. For those of ordinary skill in the art, the specific meanings of the above terms in this patent can be understood according to specific circumstances.
Claims
1. A charcoal dry distillation device, characterized in that: The invention comprises a dry distillation cellar body (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); a plurality of dry distillation tank bodies (2) are arranged in the dry distillation cellar body (1); a cover body (3) is arranged on the top of the dry distillation tank body (2); a water sealing groove (4) is arranged at the junction of the dry distillation tank body (2) and the cover body (3); one end of the main flue (10) is connected to the air inlet of the gas-liquid separator (11); the other end of the main flue (10) passes through the cover body (3) and is connected to the dry distillation tank body (2); The interior of the distillation tank body (2) is connected, the gas outlet of the gas-liquid separator (11) is connected to the gas inlet of the combustible gas check valve (13) through the auxiliary flue 1 (12), the gas outlet of the combustible gas check valve (13) is connected to the combustible gas recovery pipe (15) through the auxiliary flue 2 (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 collecting pipe (16), and the outside of the main flue (10), the gas-liquid separator (11) and the combustible gas check valve (13) is provided with a cooling device.
2. A charcoal dry distillation device as claimed in claim 1, characterized in that: The cooling device comprises 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 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 water 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) is provided with a gas-liquid separator spray pipe (22). ) is connected to the water supply pipe (18), 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), the other end of the combustible gas check valve spray pipe (23) is located above the combustible gas check valve (13), the water receiving pan (24) is located below the flue cooling tube drainage pipe (21), the gas-liquid separator (11) and the combustible gas check valve (13), and the bottom of the water receiving pan (24) is connected to the return water pipe (25).
3. A charcoal dry distillation device as claimed in claim 2, characterized in that: A water discharge pipe (5) connected to the water sealing groove (4) is arranged outside the dry distillation tank body (2), and a water discharge valve (6) is arranged on the water discharge pipe (5).
4. A charcoal dry distillation device as claimed in claim 3, characterized in that: The dry distillation cellar body (1) is provided with a heating port (8) that matches the dry distillation tank body (2), and the heating port (8) is located at the lower part of the dry distillation tank body (2).
5. A charcoal dry distillation device as claimed in claim 4, characterized in that: The cover body (3) is provided with a thermometer (7) for detecting the internal temperature of the retort tank body (2).
6. A charcoal dry distillation device as claimed in claim 5, characterized in that: The space between the retort cellar body (1) and the retort tank body (2) is filled with a heat-insulating material.
7. A charcoal dry distillation device as claimed in claim 1, characterized in that: A hanging ring (9) is provided on the top of the cover body (3).