Organic garbage treatment system
By combining a pulping machine, coarse pulp tank, integrated impurity removal machine, good pulp tank, light slag dewatering machine, and heavy slag separator, the problems of long process flow, many equipment, and high energy consumption in the treatment of kitchen waste and food waste are solved, and a highly efficient slurry impurity removal effect is achieved.
Patent Information
- Application Number
- CN202423286271.6
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-12-30
- Publication Date
- 2026-01-09
- Estimated Expiration
- 2034-12-30
AI Technical Summary
In the current treatment of food waste and kitchen waste, the pretreatment methods of mechanical pulping and hydraulic pulping have problems such as long process flow, many equipment, high energy consumption per unit pulping, and poor impurity removal effect.
The system employs a combination of a pulping machine, a coarse pulp tank, an integrated impurity removal machine, a good pulp tank, a light slag dewatering machine, and a heavy slag separator. Through multi-stage crushing, stirring, and rotary centrifugal separation, it achieves efficient impurity removal from the slurry.
The process was simplified, the number of equipment was reduced, the impurity removal effect of the slurry was improved, and energy consumption was reduced.
Smart Images

Figure CN223775660U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of waste treatment, specifically to an organic waste treatment system. Background Technology
[0002] With the advancement of waste sorting, kitchen waste and food waste are separated from household waste. Compared with household waste, kitchen waste and food waste have the characteristics of high organic matter content, high water content, and low calorific value. The organic matter in kitchen waste and food waste is treated by anaerobic fermentation to produce biogas, which has a high rate of organic matter recycling.
[0003] The above-mentioned methods for treating organic matter in kitchen waste and food waste involve mechanical pulping and hydraulic pulping as pretreatment before anaerobic fermentation. These pretreatment methods have the following drawbacks: long processing flow, numerous process equipment, poor slurry impurity removal effect, high energy consumption per unit of pulping, and numerous equipment with a high risk of failure. Utility Model Content
[0004] This invention aims to at least partially solve one of the technical problems in the aforementioned technologies. Therefore, the objective of this invention is to provide an organic waste treatment system that requires fewer processing devices, has a shorter process flow, and simultaneously ensures excellent impurity removal from the slurry.
[0005] To achieve the above objectives, this utility model proposes an organic waste treatment system, which includes: a pulping machine, a coarse pulp tank, an integrated impurity removal machine, a good pulp tank, a light residue dewatering machine, and a heavy residue separator;
[0006] The pulper is suitable for crushing and pulping organic waste and separating uncrushed light residue;
[0007] The coarse slurry tank is connected to the pulping machine to receive the slurry pumped from the pulping machine and to filter and remove impurities from the slurry;
[0008] The integrated impurity removal machine has a tank and a stirring component. The tank is provided with a feed inlet, a discharge outlet, a heavy slag outlet, and a light slag outlet. The feed inlet is connected to the coarse slurry tank so that the slurry is pumped into the tank. The stirring component is adapted to stir and break up the slurry in the tank so that the slurry rotates and separates the heavy slag and light slag. The heavy slag outlet is set away from the rotation center of the stirring component to collect the heavy slag in the slurry. The light slag outlet is set close to the rotation center of the stirring component to collect the light slag in the slurry. A first screen plate is provided at the discharge outlet.
[0009] The good pulp tank is connected to the discharge port to receive the good pulp passing through the first sieve plate and to discharge the good pulp from the good pulp outlet;
[0010] The light slag dewatering machine is connected to the pulping machine and the light slag outlet to receive the light slag discharged from the pulping machine and the integrated impurity removal machine, and to perform rotary dewatering on the received light slag. The light slag dewatering machine is connected to the coarse pulp tank to transport the slurry from which the light slag has been separated into the coarse pulp tank.
[0011] The heavy slag separator has a heavy slag tank and a separation device. The heavy slag tank is connected to the heavy slag inlet to receive the heavy slag discharged from the integrated impurity removal machine and rotates the heavy slag into the separation device. The separation device is adapted to perform solid-liquid separation on the heavy slag. The separation device is connected to the integrated impurity removal machine to transport the separated slurry into the tank.
[0012] According to the organic waste treatment system proposed in this utility model, kitchen waste material enters a pulping machine for initial crushing and refining, separating slurry and light residue. The slurry is pumped to a coarse slurry tank, where impurities are removed and then pumped to an integrated impurity removal machine. In the integrated impurity removal machine, the slurry undergoes secondary crushing and refining, separating heavy residue and light residue. The refined slurry passes through the first screen plate of the integrated impurity removal machine and is discharged into a good slurry tank, from which the good slurry is discharged. Light residue is discharged through a light residue outlet to a light residue dewatering machine for solid-liquid separation. The separated slurry flows back to the coarse slurry tank. Heavy residue is discharged through a heavy residue outlet to a heavy residue separator for solid-liquid separation, and the separated slurry flows back to the coarse slurry tank. This organic waste treatment system requires fewer processing devices, has a shorter process flow, and ensures excellent impurity removal of the slurry.
[0013] In addition, the organic waste treatment system proposed in the above embodiments of this utility model may also have the following additional technical features:
[0014] Optionally, the inlet of the feed inlet, the outlet of the good slurry outlet, and the outlet of the light slag outlet are all set higher than the tank body, and the external pipes of the good slurry outlet and the light slag outlet are all equipped with valves that can adjust the flow rate.
[0015] Furthermore, the tank is cylindrical, with one outer end of the tank recessed along the interior of the tank, and the light slag outlet is located in the recess.
[0016] Furthermore, the light slag inlet is located at the center of the concave area, and the heavy slag inlet is located at the tangent of the outer circular surface of the tank.
[0017] Furthermore, the tank is arranged horizontally.
[0018] Optionally, a scraper is connected to the agitator, and the scraper can rotate synchronously with the agitator to scrape the first sieve plate.
[0019] Optionally, the sieve holes of the first sieve plate are arranged to increase in size along its flow direction.
[0020] Optionally, the integrated impurity removal machine includes a drive unit connected to the stirring unit to drive the stirring unit to rotate.
[0021] Optionally, water pumps are provided on the external pipes between the pulper and the coarse pulp tank, the external pipes between the coarse pulp tank and the feed inlet, and the external pipes of the good pulp outlet.
[0022] Optionally, the separation device has a screw conveyor and a conveying channel adapted to the screw conveyor. A second screen plate is provided in the conveying channel. When the screw conveyor rotates, it can discharge the slurry and heavy residue and allow the slurry on the heavy residue to drip out through the second screen plate. Attached Figure Description
[0023] Figure 1 This is a schematic diagram of the organic waste treatment system according to an embodiment of the present utility model;
[0024] Figure 2 This is a partial structural schematic diagram of an organic waste treatment system according to an embodiment of the present utility model;
[0025] Figure 3 for Figure 2 A structural diagram from another perspective;
[0026] Figure 4 This is a process flow diagram of the organic waste treatment system according to an embodiment of the present utility model;
[0027] Explanation of reference numerals in the attached figures:
[0028] 1. Pulping machine; 2. Coarse pulp tank; 3. Integrated impurity removal machine; 301. Tank body; 302. Mixing component; 303. Feed inlet; 304. Discharge outlet; 305. Heavy residue outlet; 306. First screen plate; 307. Concave section; 308. Drive component; 309. Drain outlet; 310. Good pulp tank; 4. Good pulp outlet; 41. Light residue dewatering machine; 5. Heavy residue separator; 6. Heavy residue tank; 601. Separation device; 602. Pressure detection component.
[0029] 7. Water pump 8. Detailed Implementation
[0030] The embodiments of this utility model are described in detail below. Examples of these embodiments are shown in the accompanying drawings, wherein the same or similar reference numerals denote the same or similar elements or elements having the same or similar functions throughout. The embodiments described below with reference to the accompanying drawings are exemplary and intended to explain this utility model, and should not be construed as limiting this utility model.
[0031] To better understand the above technical solutions, exemplary embodiments of the present invention will be described in more detail below with reference to the accompanying drawings. Although exemplary embodiments of the present invention are shown in the drawings, it should be understood that the present invention can be implemented in various forms and should not be limited to the embodiments set forth herein. Rather, these embodiments are provided to enable a more thorough understanding of the present invention and to fully convey the scope of the present invention to those skilled in the art.
[0032] To better understand the above technical solutions, the following will provide a detailed explanation of the technical solutions in conjunction with the accompanying drawings and specific implementation methods.
[0033] The following is for reference. Figures 1-4 The implementation of the organic waste treatment system proposed in the embodiments of this utility model will be described in detail.
[0034] The organic waste treatment system according to an embodiment of the present invention includes: a pulping machine 1, a coarse pulp tank 2, an integrated impurity removal machine 3, a good pulp tank 4, a light slag dewatering machine 5, and a heavy slag separator 6.
[0035] Specifically, the pulper 1 is suitable for pulping organic waste and separating light slag; the coarse slurry tank 2 is connected to the pulper 1 to receive the slurry pumped from the pulper 1 and to filter and remove impurities from the slurry; the integrated impurity removal machine 3 has a tank 301 and an agitator 302. The tank 301 is provided with an inlet 303, an outlet 304, a heavy slag outlet 305, and a light slag outlet 306. The inlet 303 is connected to the coarse slurry tank 2 so that the slurry is pumped into the tank 301. The agitator 302 is suitable for stirring and breaking up the slurry in the tank 301 so that the slurry rotates and separates the heavy slag and light slag. The heavy slag outlet 305 is set away from the rotation center of the agitator 302 to collect the heavy slag in the slurry. The light slag outlet 306 is set close to the rotation center of the agitator 302 to collect the light slag in the slurry. The outlet 304... A first screen plate 307 is provided; a good pulp tank 4 is connected to a discharge port 304 to receive the good pulp passing through the first screen plate 307 and discharge the good pulp from the good pulp outlet 41; a light slag dewatering machine 5 is connected to a pulping machine 1 and a light slag outlet 306 to receive the light slag discharged from the pulping machine 1 and the integrated impurity removal machine 3, and to perform rotary dewatering on the received light slag; the light slag dewatering machine 5 is connected to a coarse pulp tank 2 to transport the pulp from which the light slag has been separated to the coarse pulp tank 2; a heavy slag separator 6 has a heavy slag tank 601 and a separation device 602; the heavy slag tank 601 is connected to a heavy slag outlet 305 to receive the heavy slag discharged from the integrated impurity removal machine 3, and to rotary discharge the heavy slag into the separation device 602; the separation device 602 is suitable for solid-liquid separation of the heavy slag; the separation device 602 is connected to the integrated impurity removal machine to transport the separated pulp to the tank 301.
[0036] In other words, raw kitchen waste and food scraps are fed into pulping machine 1 for crushing and refining to make pulp. The pulp is pumped through the screen plate in pulping machine 1 to coarse pulp tank 2, while the uncrushed light slag is discharged to light slag dewatering machine 5. After filtering and removing impurities in coarse pulp tank 2, the pulp is pumped from the feed inlet 303 of the impurity removal machine 3 to tank 301. The stirring element 302 in tank 301 rotates to stir and crush the pulp. Under the action of centrifugal force, light slag and heavy slag are separated from the pulp. The lighter light slag moves to the light slag outlet 306, which is closer to the stirring element 302, and is discharged into light slag dewatering machine 5 for dewatering. The slurry is returned to the coarse slurry tank 2, while the light slag is discharged from the outlet of the light slag dewatering machine 5. The heavier slag, under the action of centrifugal force, moves to the heavy slag outlet 305, which is farther away from the agitator 302, and is discharged into the heavy slag tank 601 of the heavy slag separator 6. The heavy slag tank 601 rotates to smoothly discharge the heavy slag into the separation device 602. The separation device 602 performs solid-liquid separation on the heavy slag and discharges the heavy slag. The separated slurry is returned to the coarse slurry tank 2. The remaining slurry in the tank 301 is pumped through the first screen plate 307 of the discharge port 304 and pumped into the good slurry tank 4 under the action of pumping force. The good slurry tank 4 then discharges the good slurry from the good slurry outlet 41. The pulper 1 can break down and refine organic waste through rotating blades, and the light slag in the pulper 1 can be discharged into the light slag dewatering machine 5 through a pipe; the coarse pulp tank 2 can be cleaned by using a screen plate in the coarse pulp tank 2, or it can be filtered and cleaned by a cleaning pump installed on the pipe between the coarse pulp tank 2 and the cleaning integrated machine 3.
[0037] Thus, kitchen waste enters the pulping machine 1 for initial crushing and refining, separating slurry and light slag. The slurry is pumped to the coarse slurry tank 2, where it is then pumped to the impurity removal machine 3 after impurity removal. In the impurity removal machine 3, the slurry undergoes secondary crushing and refining, separating heavy slag and light slag. The refined slurry is discharged into the good slurry tank 4 through the first screen plate 307 of the impurity removal machine 3. The good slurry is then discharged from the good slurry tank 4. The light slag is discharged through the light slag outlet 306 to the light slag dewatering machine 5 for solid-liquid separation. The separated slurry is returned to the coarse slurry tank 2. The heavy slag is discharged through the heavy slag outlet 305 into the heavy slag separator 6 for solid-liquid separation. The separated slurry is returned to the coarse slurry tank 2. This process greatly reduces the amount of equipment required, shortens the process flow, and ensures excellent impurity removal of the slurry.
[0038] Optionally, the inlet of the external pipe of the feed inlet 303, the outlet of the external pipe of the good slurry inlet 41, and the outlet of the external pipe of the light slag inlet 306 are all set higher than the tank body 301, and the external pipes of the good slurry inlet 41 and the light slag inlet 306 are all equipped with valves that can adjust the flow rate. Understandably, the above setup facilitates the formation of a pressure difference between the feed inlet 303 and the good slurry inlet 41, and between the feed inlet 303 and the light slag inlet 306. By adjusting the opening and closing degree of the valves on the external pipes of the good slurry inlet 41 and the light slag inlet 306, the flow rate of the pipes can be adjusted, thereby adjusting the pressure inside the tank 301. This ensures the smooth rotation of the slurry inside the tank 301 and improves the separation efficiency of light slag, heavy slag, and good slurry. Both the external pipes of the feed inlet 303 and the good slurry inlet 41 are equipped with pressure detection devices 7 to detect the pressure inside the pipes, making it easy to observe the pressure in the external pipes of the feed inlet 303 and the good slurry inlet 41, thus facilitating the protection of the overall device operation. The pressure detection device 7 can be a pressure sensor or a pressure gauge.
[0039] Furthermore, the tank 301 is cylindrical, with one outer end of the tank 301 positioned along the inner first screen plate 308. A light slag outlet 306 is located at the first screen plate 308. Understandably, the cylindrical shape of the tank 301 and the placement of the first screen plate 308 facilitate better coordination with the rotation of the agitator 302, enabling the slurry to rapidly rotate and separate heavy and light slag. The placement of the light slag outlet 306 at the first screen plate 308 increases the contact area between the first screen plate 308 and the light slag, thus facilitating the collection and discharge of the light slag and guiding it to the outlet 306. The agitator 302 may extend from the opposite end of the first screen plate 308 towards the first screen plate 308, and the agitator 302 is equipped with blades.
[0040] Furthermore, the light slag inlet 306 is located at the center of the first screen plate 308, and the heavy slag inlet 305 is located at the tangent of the outer circular surface of the tank body 301. Understandably, by placing the light slag inlet 306 at the center of the first screen plate 308 and the heavy slag inlet 305 at the tangent of the outer circular surface of the tank body 301, the distribution positions of the heavy and light slag after centrifugal motion can be better matched, thereby facilitating the collection and discharge of medium-heavy and light slag, and thus improving the impurity removal efficiency of the slurry. Valves are installed on the external pipes of both the light slag inlet 306 and the heavy slag inlet 305.
[0041] Furthermore, the tank 301 is arranged horizontally. Understandably, the horizontal arrangement of the tank 301 facilitates the flattening of the overall device, thereby reducing the space occupied by the overall device. At the same time, it can prevent heavy and light slag from accumulating at the bottom, which would result in poor separation effect when the device is set vertically.
[0042] Optionally, a scraper is connected to the agitator 302, which rotates synchronously with the agitator 302 to scrape the first screen plate 307. Understandably, the scraper facilitates the removal of material adhering to or clogging the first screen plate 307, thereby preventing clogging and ensuring efficient discharge of good slurry and the overall operation of the device. The agitator 302 can pass through the center of the screen plate, and the first screen plate 307 can be circular to allow for more thorough scraping by the rotating scraper.
[0043] Optionally, the sieve holes of the first sieve plate 307 are arranged to gradually increase in size along its flow direction. Understandably, by arranging the sieve holes of the first sieve plate 307 to gradually increase in size along its flow direction, it is easier to increase the speed at which the slurry passes through the sieve holes while maintaining the filtration effect of the first sieve plate 307, thereby improving the filtration efficiency. The sieve holes can be stepped holes with varying diameters or conical holes.
[0044] Optionally, the integrated impurity removal machine 3 includes a drive unit 309, which is connected to the agitator 302 to drive the agitator 302 to rotate. Understandably, connecting the agitator 302 to the drive unit 309 facilitates the rotation of the agitator 302, thereby facilitating the rotational movement of the slurry within the tank 301. The drive unit 309 can be a structure consisting of a motor, belt, and pulley.
[0045] Optionally, water pumps 8 are installed on the external pipes between the pulper 1 and the coarse pulp tank 2, the external pipes between the coarse pulp tank 2 and the feed inlet 303, and the external pipes connecting to the good pulp outlet 41. Understandably, by installing water pumps 8, the flow rate and power of the slurry after organic waste pulping can be increased between the coarse pulp tank 2, the integrated impurity removal machine 3, and the good pulp tank 4, thereby ensuring the discharge efficiency of good pulp and the separation efficiency of light and heavy slag. Specifically, the water pump 8 on the pipe between the coarse pulp tank 2 and the integrated impurity removal machine 3 can be an impurity removal pump, and water pumps 8 can be installed on the external pipes through which slurry flows between each device to ensure the slurry transport efficiency.
[0046] Optionally, the separation device 602 has a screw conveyor and a conveying channel adapted to the screw conveyor. A second screen plate is provided within the conveying channel. When the screw conveyor rotates, it discharges the heavy slag and allows the slurry on the heavy slag to drain through the second screen plate. Understandably, by cooperating with the second screen plate within the conveying channel, the heavy slag can fully contact and roll with the second screen plate during the rotation of the screw conveyor, thereby facilitating the separation of the slurry from the heavy slag and its drainage through the screen openings of the second screen plate. The drained slurry is collected and then pumped back to the coarse slurry tank 2, avoiding waste of slurry. The heavy slag discharge outlet of the separation device 602 can be inclined upwards.
[0047] In addition, a drain port 310 is provided at the bottom of the tank 301. Understandably, the drain port 310 facilitates the discharge of substances other than heavy slag, light slag, and good liquid, thereby ensuring the cleanliness and operation of the entire unit. The external pipeline of the drain port 310 is equipped with an automatic valve, facilitating switching between continuous and batch operation of the entire unit. When there is little light slag in the slurry, the light slag can be discharged from the drain port 310 by closing the valve.
[0048] In the description of this utility model, it should be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", etc., indicating the orientation or positional relationship are based on the orientation or positional relationship shown in the accompanying drawings, and are only for the convenience of describing this utility model and simplifying the description, and are not intended to indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation, and therefore should not be construed as a limitation of this utility model.
[0049] Furthermore, the terms "first" and "second" are used for descriptive purposes only and should not be construed as indicating or implying relative importance or implicitly specifying the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature. In the description of this utility model, "a plurality of" means two or more, unless otherwise explicitly specified.
[0050] In this utility model, unless otherwise explicitly specified and limited, the terms "installation," "connection," "joining," and "fixing," etc., should be interpreted broadly. For example, they can refer to a fixed connection, a detachable connection, or an integral part; they can refer to a mechanical connection or an electrical connection; they can refer to a direct connection or an indirect connection through an intermediate medium; they can refer to a connection within two components or an interaction 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.
[0051] In this invention, unless otherwise explicitly specified and limited, "above" or "below" the second feature can include direct contact between the first and second features, or contact between the first and second features through another feature between them. Furthermore, "above," "over," and "on top" of the second feature includes the first feature directly above or diagonally above the second feature, or simply indicates that the first feature is at a higher horizontal level than the second feature. "Below," "below," and "under" the second feature includes the first feature directly below or diagonally below the second feature, or simply indicates that the first feature is at a lower horizontal level than the second feature.
[0052] In the description of this specification, the references to terms such as "one embodiment," "some embodiments," "example," "specific example," or "some examples," etc., indicate that a specific feature, structure, material, or characteristic described in connection with that embodiment or example is included in at least one embodiment or example of the present invention. The illustrative expressions of the above terms in this specification should not be construed as necessarily referring to the same embodiment or example. Furthermore, the specific features, structures, materials, or characteristics described may be combined in any suitable manner in one or more embodiments or examples. In addition, those skilled in the art can combine and integrate the different embodiments or examples described in this specification.
[0053] Although embodiments of the present invention have been shown and described above, it is understood that the above embodiments are exemplary and should not be construed as limiting the present invention. Those skilled in the art can make changes, modifications, substitutions and variations to the above embodiments within the scope of the present invention.
Claims
1. An organic waste treatment system, characterized in that, include: Pulping machine, coarse pulp tank, integrated impurity removal machine, good pulp tank, light residue dewatering machine and heavy residue separator; The pulper is suitable for crushing and pulping organic waste and separating uncrushed light residue; The coarse slurry tank is connected to the pulping machine to receive the slurry pumped from the pulping machine and to filter and remove impurities from the slurry; The integrated impurity removal machine has a tank and a stirring component. The tank is provided with a feed inlet, a discharge outlet, a heavy slag outlet, and a light slag outlet. The feed inlet is connected to the coarse slurry tank so that the slurry is pumped into the tank. The stirring component is adapted to stir and break up the slurry in the tank so that the slurry rotates and separates the heavy slag and light slag. The heavy slag outlet is set away from the rotation center of the stirring component to collect the heavy slag in the slurry. The light slag outlet is set close to the rotation center of the stirring component to collect the light slag in the slurry. A first screen plate is provided at the discharge outlet. The good pulp tank is connected to the discharge port to receive the good pulp passing through the first sieve plate and to discharge the good pulp from the good pulp outlet; The light slag dewatering machine is connected to the pulping machine and the light slag outlet to receive the light slag discharged from the pulping machine and the integrated impurity removal machine, and to perform rotary dewatering on the received light slag. The light slag dewatering machine is connected to the coarse pulp tank to transport the slurry from which the light slag has been separated into the coarse pulp tank. The heavy slag separator has a heavy slag tank and a separation device. The heavy slag tank is connected to the heavy slag inlet to receive the heavy slag discharged from the integrated impurity removal machine and rotates the heavy slag into the separation device. The separation device is adapted to perform solid-liquid separation on the heavy slag. The separation device is connected to the integrated impurity removal machine to transport the separated slurry into the tank.
2. The organic waste treatment system as described in claim 1, characterized in that, The inlet of the feed inlet, the outlet of the good slurry outlet, and the outlet of the light slag outlet are all set higher than the tank body, and the external pipes of the good slurry outlet and the light slag outlet are all equipped with valves that can adjust the flow rate.
3. The organic waste treatment system as described in claim 1 or 2, characterized in that, The tank is cylindrical, with one outer end of the tank recessed along the interior of the tank, and the light slag outlet is located in the recess.
4. The organic waste treatment system as described in claim 3, characterized in that, The light slag inlet is located at the center of the concave area, and the heavy slag inlet is located at the tangent of the outer circular surface of the tank.
5. The organic waste treatment system as described in claim 4, characterized in that, The tank is set horizontally.
6. The organic waste treatment system as described in claim 1, characterized in that, A scraper is connected to the agitator, and the scraper can rotate synchronously with the agitator to scrape the first sieve plate.
7. The organic waste treatment system as described in claim 1, characterized in that, The sieve holes of the first sieve plate are arranged to increase in size along its flow direction.
8. The organic waste treatment system as described in claim 1, characterized in that, The integrated impurity removal machine includes a drive unit, which is connected to the stirring unit to drive the stirring unit to rotate.
9. The organic waste treatment system as described in claim 1, characterized in that, Water pumps are installed on the external pipes connecting the pulper and the coarse pulp tank, the external pipes connecting the coarse pulp tank and the feed inlet, and the external pipes connecting the good pulp inlet.
10. The organic waste treatment system as described in claim 1, characterized in that, The separation device has a screw conveyor and a conveying channel adapted to the screw conveyor. A second screen plate is provided in the conveying channel. When the screw conveyor rotates, it can discharge the slurry and heavy residue and allow the slurry on the heavy residue to drip out of the second screen plate.