Self-propelled precision collaborative regulation intelligent compost reactor
By setting up low-oxygen, normal-oxygen, and ultra-low-oxygen zones in the composting reactor and using sensors and control devices for precise oxygen concentration regulation, the problems of unsatisfactory material fermentation, low humification, and high energy consumption in the composting reactor have been solved, achieving a more efficient composting process.
Patent Information
- Application Number
- CN202510577458.1
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2025-05-06
- Publication Date
- 2025-11-21
- Estimated Expiration
- 2045-05-06
AI Technical Summary
Existing composting reactors have unsatisfactory material fermentation effects, low humification levels, significant nutrient loss, and high energy consumption, and lack precise oxygen concentration control at different fermentation stages.
Design a self-propelled, precise, and collaboratively controlled intelligent composting reactor, comprising a low-oxygen zone, a normal-oxygen zone, and an ultra-low-oxygen zone, equipped with oxygen concentration, temperature, and moisture sensors. The aeration rate is adjusted according to the real-time material temperature and moisture content by a control device to achieve precise control of different oxygen concentration zones.
It improves composting fermentation efficiency, increases humification, reduces nutrient loss, and lowers energy consumption.
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Figure CN120504557B_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The present application relates to the technical field of composting, in particular to a self-moving precise synergistic regulation intelligent composting reactor. BACKGROUND
[0002] With the continuous expansion of livestock and poultry breeding scale, the amount of livestock and poultry manure is rapidly increasing. Composting is a common way to convert livestock and poultry manure into organic fertilizer, which realizes the resource utilization of livestock and poultry manure. Among them, the aerobic composting technology is biodegradable, which can decompose and convert the organic waste in livestock and poultry manure into stable humus substances under aerobic conditions through the metabolic activity of microorganisms.
[0003] The composting reactor is a device specially used for composting. The composting reactor is usually an aerobic zone. The oxygen concentration of the aerobic zone needs to be controlled during the composting process. In the related technology, a threshold value of the oxygen concentration of the aerobic zone is set. During the composting process, the oxygen concentration in the aerobic zone is detected, and the aeration amount of the aerobic zone is controlled according to the detection value of the oxygen concentration and the set threshold value, until the detection value of the oxygen concentration of the aerobic zone is consistent with the set threshold value. Although the regulation of the oxygen concentration of the aerobic zone is realized, the set threshold value of the oxygen concentration is a fixed value, which has a large difference with the oxygen concentration required by each fermentation stage, resulting in an unsatisfactory fermentation effect of the composting material. In addition, the reactor is mostly in a strong aeration state (to maintain an aerobic state), lacks a pretreatment stage of the composting raw material, and the strong aeration in the later stage of composting (cooling and maturation stage) will cause a large loss of nutrients, which is not conducive to achieving a better humification level, and the high aeration amount used in the whole composting process also leads to high operating cost and energy consumption.
[0004] Therefore, how to solve the problems of the composting reactor in the related technology, such as unsatisfactory fermentation effect of the material, low humification degree, large nutrient loss and high energy consumption, has become an important technical problem to be solved by the technical personnel in the field. SUMMARY
[0005] The present application provides a self-moving precise synergistic regulation intelligent composting reactor to solve the defects of the composting reactor in the related technology, such as unsatisfactory fermentation effect of the material, low humification degree, large nutrient loss and high energy consumption.
[0006] The present application provides a self-moving precise synergistic regulation intelligent composting reactor, comprising:
[0007] The reactor body has a low-oxygen zone, a normal-oxygen zone and a super-low-oxygen zone distributed in sequence inside, and the low-oxygen zone and the super-low-oxygen zone are both communicated with the normal-oxygen zone;
[0008] An aeration device adapted to aerate the material in the low-oxygen zone, the normal-oxygen zone and the ultra-low-oxygen zone, respectively;
[0009] An oxygen concentration sensor comprising a low-oxygen zone oxygen concentration sensor adapted to detect the oxygen concentration in the material in the low-oxygen zone, a normal-oxygen zone oxygen concentration sensor adapted to detect the oxygen concentration in the material in the normal-oxygen zone, and an ultra-low-oxygen zone oxygen concentration sensor adapted to detect the oxygen concentration in the material in the ultra-low-oxygen zone;
[0010] A normal-oxygen zone temperature sensor adapted to detect the temperature of the material in the normal-oxygen zone;
[0011] A normal-oxygen zone moisture sensor adapted to detect the moisture content of the material in the normal-oxygen zone;
[0012] A control device, the aeration device, the low-oxygen zone oxygen concentration sensor, the normal-oxygen zone oxygen concentration sensor, the ultra-low-oxygen zone oxygen concentration sensor, the normal-oxygen zone temperature sensor and the normal-oxygen zone moisture sensor are electrically connected to the control device, the control device is adapted to determine the current time set value of the oxygen concentration in the material in the normal-oxygen zone according to the current time temperature of the material in the normal-oxygen zone and the current time moisture content of the material in the normal-oxygen zone, and control the aeration device according to the current time set value of the oxygen concentration and the current time temperature of the material in the normal-oxygen zone.
[0013] According to the self-propelled precise cooperative regulation intelligent compost reactor provided by the application, the relationship between the current time temperature of the material in the normal-oxygen zone, the current time moisture content of the material in the normal-oxygen zone and the current time set value of the oxygen concentration in the material in the normal-oxygen zone is C1=a×WC-b×T1+e, wherein C1 is the current time set value of the oxygen concentration in the material in the normal-oxygen zone, WC is the current time moisture content of the material in the normal-oxygen zone, T1 is the current time temperature of the material in the normal-oxygen zone, a, b and e are all constants;
[0014] The control device is further adapted to determine the current time set range of the oxygen concentration according to the current time set value of the oxygen concentration, and control the aeration device according to the current time set range of the oxygen concentration, the lower limit value of the current time set range is 95% of the current time set value of the oxygen concentration, and the upper limit value of the current time set range is 105% of the current time set value of the oxygen concentration.
[0015] According to the self-moving precise cooperative regulation intelligent compost reactor provided by the application, the control device is further adapted to control the aeration device according to the oxygen concentration in the material in the low-oxygen zone and the set range of the oxygen concentration in the material in the low-oxygen zone, and the set range of the oxygen concentration in the material in the low-oxygen zone is 3% to 5%;
[0016] The control device is further adapted to control the aeration device according to the oxygen concentration in the material in the ultra-low-oxygen zone and the set range of the oxygen concentration in the material in the ultra-low-oxygen zone, and the set range of the oxygen concentration in the material in the ultra-low-oxygen zone is 1% to 3%.
[0017] According to the self-moving precise cooperative regulation intelligent compost reactor provided by the application, the aeration device comprises:
[0018] An aerator is arranged outside the reactor body;
[0019] An aeration pipeline is arranged inside the reactor body and at the bottom of the reactor body, and the side wall of the aeration pipeline is provided with aeration holes distributed at intervals;
[0020] A first connecting pipeline is arranged outside the reactor body, and the first connecting pipeline connects the aeration pipeline and the aerator;
[0021] The reactor body comprises:
[0022] A box body has an accommodating space inside;
[0023] A partition plate assembly is arranged at the bottom of the box body, and a spacing is formed between the partition plate assembly and the bottom wall of the box body to form an aeration cavity, a plurality of communication holes distributed at intervals are arranged on the partition plate assembly, and the communication holes are arranged to be adapted to allow only the gas in the aeration cavity to flow upwards of the partition plate assembly;
[0024] A partition assembly is arranged in the aeration cavity, and the partition assembly is adapted to divide the aeration cavity into a micro-aerobic aeration cavity, an aerobic aeration cavity and a low-oxygen aeration cavity, the micro-aerobic aeration cavity is located below the low-oxygen zone, the aerobic aeration cavity is located below the normal-oxygen zone, and the low-oxygen aeration cavity is located below the ultra-low-oxygen zone;
[0025] The aeration pipeline comprises:
[0026] A first aeration pipeline is arranged in the micro-aerobic aeration cavity;
[0027] A second aeration pipeline is arranged in the aerobic aeration cavity;
[0028] A third aeration pipeline is arranged in the low-oxygen aeration cavity;
[0029] The first connecting pipeline has three branch pipelines, the three branch pipelines are connected with the first aeration pipeline, the second aeration pipeline and the third aeration pipeline respectively, the first control valve and the flow meter are arranged on the three branch pipelines, the first control valve is suitable for controlling the on-off state of the branch pipeline and adjusting the flow in the branch pipeline, and the flow meter and the first control valve are electrically connected with the control device.
[0030] According to the self-propelled intelligent composting reactor, the separation plate assembly comprises:
[0031] The low-oxygen-zone separation plate is located above the micro-aerobic aeration cavity, is detachably connected with the box body, the diameter of the communication hole on the low-oxygen-zone separation plate is 2-5 mm, and the opening rate of the low-oxygen-zone separation plate is 10%-20%.
[0032] The normal-oxygen-zone separation plate is located above the aerobic aeration cavity, is detachably connected with the box body, the diameter of the communication hole on the normal-oxygen-zone separation plate is 5-10 mm, and the opening rate of the normal-oxygen-zone separation plate is 20%-50%.
[0033] The ultra-low-oxygen-zone separation plate is located above the low-oxygen aeration cavity, is detachably connected with the box body, the diameter of the communication hole on the ultra-low-oxygen-zone separation plate is 2-5 mm, and the opening rate of the ultra-low-oxygen-zone separation plate is 10%-20%.
[0034] According to the self-propelled intelligent composting reactor, the reactor body is internally provided with a stirring device, and a lifting mechanism is arranged between the low-oxygen-zone oxygen concentration sensor and the top wall of the reactor body, between the normal-oxygen-zone oxygen concentration sensor and the top wall of the reactor body, between the ultra-low-oxygen-zone oxygen concentration sensor and the top wall of the reactor body, between the normal-oxygen-zone temperature sensor and the top wall of the reactor body, and between the normal-oxygen-zone moisture sensor and the top wall of the reactor body.
[0035] The stirring device and the lifting mechanism are electrically connected with the control device, the control device is suitable for controlling the low-oxygen-zone oxygen concentration sensor, the normal-oxygen-zone oxygen concentration sensor, the ultra-low-oxygen-zone oxygen concentration sensor, the normal-oxygen-zone temperature sensor and the normal-oxygen-zone moisture sensor to rise to the top of the reactor body when the stirring device operates, and controlling the low-oxygen-zone oxygen concentration sensor, the normal-oxygen-zone oxygen concentration sensor, the ultra-low-oxygen-zone oxygen concentration sensor, the normal-oxygen-zone temperature sensor and the normal-oxygen-zone moisture sensor to descend to immerse in the material when the stirring device stops operating.
[0036] According to the application, a self-moving precise cooperative control intelligent composting reactor is provided, wherein the stirring device comprises:
[0037] a support base adapted to move along the longitudinal direction of the reactor body relative to the reactor body;
[0038] a first driving mechanism adapted to drive the support base to move along the longitudinal direction of the reactor body, the first driving mechanism being electrically connected with the control device;
[0039] a mounting base provided on the support base, the mounting base being adapted to move along the transverse direction of the reactor body relative to the support base;
[0040] a second driving mechanism adapted to drive the mounting base to move along the transverse direction of the reactor body, the second driving mechanism being electrically connected with the control device;
[0041] a spiral stirring mechanism provided on the mounting base, a spiral stirring shaft of the spiral stirring mechanism being adapted to rotate about its own axis relative to the mounting base, the spiral stirring shaft being obliquely arranged relative to the bottom wall of the reactor body, the spiral stirring mechanism being electrically connected with the control device;
[0042] a scraper located below the spiral stirring shaft, the scraper being fixed relative to the mounting base, the scraper being adapted to scrape off the materials on the bottom wall of the low-oxygen zone, the bottom wall of the normal-oxygen zone and the bottom wall of the ultra-low-oxygen zone.
[0043] According to the application, a self-moving precise cooperative control intelligent composting reactor is provided, wherein the stirring device further comprises:
[0044] a stirring oxygen concentration sensor provided on the spiral stirring mechanism, the stirring oxygen concentration sensor being adapted to detect the oxygen concentration in the materials around the spiral stirring mechanism in real time when the stirring device is running, so as to determine the region where the spiral stirring mechanism is located, and then control the rotating speed of the spiral stirring mechanism;
[0045] when the spiral stirring mechanism is in the low-oxygen zone, the spiral stirring mechanism is controlled to rotate 10-20 times per minute; when the spiral stirring mechanism is in the normal-oxygen zone, the spiral stirring mechanism is controlled to rotate 20-30 times per minute; and when the spiral stirring mechanism is in the ultra-low-oxygen zone, the spiral stirring mechanism is controlled to rotate 5-10 times per minute.
[0046] According to the application, a self-moving precise cooperative control intelligent composting reactor is provided, wherein the two ends of the transverse direction of the support base are respectively provided with first support guide mechanisms relative to the reactor body, the first support guide mechanisms comprising:
[0047] A first guide slot is arranged on the reactor body and extends along the longitudinal direction of the reactor body;
[0048] A first roller is rotatably arranged on the support seat, and the rolling axis of the first roller is arranged along the transverse direction of the reactor body.
[0049] The first driving mechanism comprises:
[0050] A first rack is arranged on the reactor body and extends along the longitudinal direction of the reactor body;
[0051] A first gear is in meshing transmission with the first rack, and the first gear is rotatably arranged on the support seat, and the axis of the first gear is arranged along the vertical direction of the reactor body;
[0052] A first driving member is arranged on the support seat, and the first driving member is in transmission connection with the first gear, and the first driving member is electrically connected with the control device.
[0053] According to the self-propelled intelligent compost reactor provided by the application, the longitudinal two ends of the mounting seat and the support seat are provided with a second support guide mechanism, and the second support guide mechanism comprises:
[0054] A second guide slot is arranged on the support seat and extends along the transverse direction of the reactor body;
[0055] A second roller is rotatably arranged on the mounting seat, and the rolling axis of the second roller is arranged along the longitudinal direction of the reactor body.
[0056] The second driving mechanism comprises:
[0057] A second rack is arranged on the support seat and extends along the transverse direction of the reactor body;
[0058] A second gear is in meshing transmission with the second rack, and the second gear is rotatably arranged on the mounting seat, and the axis of the second gear is arranged along the vertical direction of the reactor body;
[0059] A second driving member is arranged on the mounting seat, and the second driving member is in transmission connection with the second gear, and the second driving member is electrically connected with the control device.
[0060] The application provides a self-propelled precise synergistic control intelligent composting reactor, which comprises a reactor body, an aeration device, an oxygen concentration sensor, a normal-oxygen-zone temperature sensor, a normal-oxygen-zone moisture sensor and a control device. The interior of the reactor body has a low-oxygen zone, a normal-oxygen zone and an ultralow-oxygen zone arranged in sequence, the low-oxygen zone and the ultralow-oxygen zone are both communicated with the normal-oxygen zone, the material in the low-oxygen zone can move to the normal-oxygen zone, and the material in the normal-oxygen zone can move to the ultralow-oxygen zone. The oxygen concentration sensor comprises a low-oxygen-zone oxygen concentration sensor, a normal-oxygen-zone oxygen concentration sensor and an ultralow-oxygen-zone oxygen concentration sensor, the low-oxygen-zone oxygen concentration sensor is used for detecting the oxygen concentration in the material in the low-oxygen zone, the normal-oxygen-zone oxygen concentration sensor is used for detecting the oxygen concentration in the material in the normal-oxygen zone, and the ultralow-oxygen-zone oxygen concentration sensor is used for detecting the oxygen concentration in the material in the ultralow-oxygen zone. The aeration device can aerate the materials in the low-oxygen zone, the normal-oxygen zone and the ultralow-oxygen zone respectively to provide appropriate oxygen for the low-oxygen zone, the normal-oxygen zone and the ultralow-oxygen zone. The normal-oxygen-zone temperature sensor is used for detecting the temperature of the material in the normal-oxygen zone, and the normal-oxygen-zone moisture sensor is used for detecting the moisture content of the material in the normal-oxygen zone. The aeration device, the low-oxygen-zone oxygen concentration sensor, the normal-oxygen-zone oxygen concentration sensor, the ultralow-oxygen-zone oxygen concentration sensor, the normal-oxygen-zone temperature sensor and the normal-oxygen-zone moisture sensor are all electrically connected with the control device. The control device can control the aeration of the aeration device in each zone according to the oxygen concentration in the material in each zone. The temperature and the moisture content of the material in the normal-oxygen zone can indirectly reflect the degradation process of the organic matter in the normal-oxygen zone. When the material in the normal-oxygen zone is aerated, the current time set value of the oxygen concentration in the material in the normal-oxygen zone is determined according to the current time temperature of the material in the normal-oxygen zone and the current time moisture content of the material in the normal-oxygen zone, and the aeration device is controlled according to the current time set value of the oxygen concentration and the current time oxygen concentration of the material in the normal-oxygen zone. In this way, according to the real-time situation of the normal-oxygen zone, the real-time demand of the normal-oxygen zone for the oxygen concentration is determined, the real-time demand of the normal-oxygen zone for the oxygen concentration is set as the set value of the oxygen concentration of the normal-oxygen zone in real time, and then the aeration amount of the aeration device is controlled according to the real-time detection value of the normal-oxygen-zone oxygen concentration sensor and the set value of the oxygen concentration of the normal-oxygen zone set in real time, thereby improving the consistency between the set value of the oxygen concentration of the normal-oxygen zone and the real-time actual demand of the normal-oxygen zone for the oxygen concentration, effectively ensuring the fermentation effect of the normal-oxygen zone and solving the problems of the material fermentation effect of the composting reactor in the related art, such as low humification degree, large nutrient loss and high energy consumption. BRIEF DESCRIPTION OF DRAWINGS
[0061] In order to make the technical solutions in the present application or the prior art clearer, the accompanying drawings needed in the embodiments or the prior art description will be briefly introduced below. Obviously, the accompanying drawings in the following description are only some embodiments of the present application, and other accompanying drawings can be obtained by those skilled in the art without any creative effort based on these accompanying drawings.
[0062] Figure 1 is a front view of the self-propelled precise cooperative control intelligent composting reactor provided by the present application (the stirring device is not shown in the figure).
[0063] Figure 2 is a top view of the self-propelled precise cooperative control intelligent composting reactor provided by the present application.
[0064] Figure 3 is a side view of the self-propelled precise cooperative control intelligent composting reactor provided by the present application.
[0065] Figure 4 is a front view of the aeration cavity provided by the present application.
[0066] Figure 5 is a top view of the aeration cavity provided by the present application.
[0067] Figure 6 is a top view of the first support guide mechanism and the second support guide mechanism provided by the present application.
[0068] Figure 7 is a side view of the first support guide mechanism provided by the present application.
[0069] Figure 8 is a structural schematic view of the feeding device provided by the present application.
[0070] Reference signs:
[0071] 1. Low-oxygen zone; 2. Normal-oxygen zone; 3. Ultra-low-oxygen zone; 4. Oxygen concentration sensor for normal-oxygen zone; 5. Temperature sensor for normal-oxygen zone; 6. Control device; 7. Low-oxygen zone partition plate; 8. Oxygen concentration sensor for ultra-low-oxygen zone; 9. Normal-oxygen zone partition plate; 10. Aerator; 11. First connecting pipe; 12. Housing; 13. Ultra-low-oxygen zone partition plate; 14. Micro-oxygen aeration chamber; 15. Aerobic aeration chamber; 16. Low-oxygen aeration chamber; 17. Oxygen concentration sensor for low-oxygen zone; 18. First aeration pipe; 19. Second aeration pipe; 20. Third aeration pipe; 21. First control device. 21. Valve; 22. Flow meter; 23. Moisture sensor for normal oxygen zone; 24. Support base; 25. Mounting base; 26. Spiral stirring mechanism; 27. Spiral stirring shaft; 28. Scraper; 29. First guide groove; 30. First roller; 31. First rack; 32. First gear; 33. Second guide groove; 34. Second roller; 35. Second rack; 36. Second gear; 37. First driving component; 38. Second driving component; 39. Separator bar; 40. Support block; 41. Conveying device; 42. Guide bracket; 43. Connecting bracket; 44. Sprocket; 45. Chain. Detailed Implementation
[0072] To make the objectives, technical solutions, and advantages of this invention clearer, the technical solutions of this invention will be clearly and completely described below with reference to the accompanying drawings. Obviously, the described embodiments are only some, not all, of the embodiments of this invention. All other embodiments obtained by those skilled in the art based on the embodiments of this invention without creative effort are within the scope of protection of this invention.
[0073] The following is combined with Figures 1 to 8 This invention describes a self-propelled, precisely coordinated, and intelligent composting reactor.
[0074] like Figures 1 to 8 As shown, the self-propelled, precise, and collaboratively controlled intelligent composting reactor provided in this embodiment of the invention includes a reactor body, an aeration device, an oxygen concentration sensor, a normal oxygen zone temperature sensor 5, a normal oxygen zone moisture sensor 23, and a control device 6.
[0075] Specifically, the reactor body has a low-oxygen zone 1, a normal-oxygen zone 2, and an ultra-low-oxygen zone 3 distributed sequentially inside. Both the low-oxygen zone 1 and the ultra-low-oxygen zone 3 are connected to the normal-oxygen zone 2. Materials in the low-oxygen zone 1 can move to the normal-oxygen zone 2, and materials in the normal-oxygen zone 2 can move to the ultra-low-oxygen zone 3.
[0076] The low-oxygen zone 1 and the ultra-low-oxygen zone 3 are added on the basis of the normal-oxygen zone 2. The pretreatment stage is carried out in the low-oxygen zone 1, which can make some complex or refractory organic matter degraded, provide a large amount of easily degradable small molecular organic matter, and preserve some aerobic microorganisms, thus laying a foundation for the aerobic fermentation, making the temperature rise faster, and making the fermentation effect of the refractory or complex organic matter better. The temperature reduction and composting stages are carried out in the ultra-low-oxygen zone 3, and most of the organic matter is decomposed in the later stage of composting, so that high aeration is not needed. When the micro-aeration is carried out, not only the aerobic microorganisms, but also the facultative microorganisms and the anaerobic microorganisms can survive, so that the refractory or complex organic matter can be degraded again. The ultra-low-oxygen zone 3 can achieve a better humification level.
[0077] The oxygen concentration sensors include the low-oxygen zone oxygen concentration sensor 17, the normal-oxygen zone oxygen concentration sensor 4, and the ultra-low-oxygen zone oxygen concentration sensor 8. The low-oxygen zone oxygen concentration sensor 17 is used to detect the oxygen concentration in the material in the low-oxygen zone 1, the normal-oxygen zone oxygen concentration sensor 4 is used to detect the oxygen concentration in the material in the normal-oxygen zone 2, and the ultra-low-oxygen zone oxygen concentration sensor 8 is used to detect the oxygen concentration in the material in the ultra-low-oxygen zone 3.
[0078] The aeration device can aerate the material in the low-oxygen zone 1, the normal-oxygen zone 2, and the ultra-low-oxygen zone 3 respectively, so as to provide appropriate oxygen for the low-oxygen zone 1, the normal-oxygen zone 2, and the ultra-low-oxygen zone 3 respectively.
[0079] The normal-oxygen zone temperature sensor 5 is used to detect the temperature of the material in the normal-oxygen zone 2, and the normal-oxygen zone moisture sensor 23 is used to detect the moisture content of the material in the normal-oxygen zone 2.
[0080] The aeration device, the low-oxygen zone oxygen concentration sensor 17, the normal-oxygen zone oxygen concentration sensor 4, the ultra-low-oxygen zone oxygen concentration sensor 8, the normal-oxygen zone temperature sensor 5, and the normal-oxygen zone moisture sensor 23 are electrically connected with the control device 6. The control device 6 can control the aeration of the aeration device in each zone according to the oxygen concentration in the material in each zone.
[0081] The temperature and the moisture content of the material in the normal-oxygen zone 2 can indirectly reflect the degradation process of the organic matter in the normal-oxygen zone 2. When the material in the normal-oxygen zone 2 is aerated, the current time set value of the oxygen concentration in the material in the normal-oxygen zone 2 is determined according to the current time temperature of the material in the normal-oxygen zone 2 and the current time moisture content of the material in the normal-oxygen zone 2, and the aeration device is controlled according to the current time set value of the oxygen concentration and the current time oxygen concentration of the material in the normal-oxygen zone 2.
[0082] In this way, the real-time demand of the aerobic zone 2 for the oxygen concentration is determined according to the real-time condition of the aerobic zone 2, the real-time demand of the aerobic zone 2 for the oxygen concentration is set as the set value of the oxygen concentration of the aerobic zone 2 in real time, and then the aeration amount of the aeration device is controlled according to the real-time detection value of the aerobic zone oxygen concentration sensor 4 and the set value of the oxygen concentration of the aerobic zone 2 set in real time, so that the consistency of the set value of the oxygen concentration of the aerobic zone 2 and the real-time actual demand of the aerobic zone 2 for the oxygen concentration is improved, the fermentation effect of the aerobic zone 2 can be effectively ensured, and the problems of the material fermentation effect of the composting reactor being not ideal, the humification degree being low, the nutrient loss being large, and the energy consumption being high in the related art are solved.
[0083] In the embodiment of the present application, the relationship among the current time temperature of the material in the aerobic zone 2, the current time moisture content of the material in the aerobic zone 2, and the current time set value of the oxygen concentration in the material in the aerobic zone 2 is C1=a*WC-b*T1+e. Wherein, C1 is the current time set value of the oxygen concentration in the material in the aerobic zone 2, the unit of C1 is percentage (symbol %), WC is the current time moisture content of the material in the aerobic zone 2, the unit of WC is percentage (symbol %), T1 is the current time temperature of the material in the aerobic zone 2, the unit of T1 is Celsius (symbol ℃). a, b and e are all constants, which can be determined through multiple tests. In some embodiments, according to the test, a=3.366, b=0.198, and e=22.336.
[0084] The current time temperature T1 of the material in the aerobic zone 2 is detected by the aerobic zone temperature sensor 5, the current time moisture content of the material in the aerobic zone 2 is detected by the aerobic zone moisture sensor 23, and the current time set value C1 of the oxygen concentration in the material in the aerobic zone 2 is calculated and determined according to the above relationship C1=a*WC-b*T1+e. At the same time, the oxygen concentration in the material in the aerobic zone 2 is detected in real time by the aerobic zone oxygen concentration sensor 4, and the aeration amount of the aeration device at the current time is controlled according to the detected oxygen concentration in the material in the aerobic zone 2 and the current time set value C1 of the oxygen concentration in the material in the aerobic zone 2 calculated and determined.
[0085] Specifically, when the aeration device is controlled according to the current time set value of the oxygen concentration and the current time oxygen concentration of the material in the aerobic zone 2, the current time setting range of the oxygen concentration can be determined according to the current time set value of the oxygen concentration. Then the aeration device is controlled according to the current time setting range of the oxygen concentration.
[0086] The oxygen concentration set value corresponding to each time is a numerical range, which is more convenient for control.
[0087] In a specific embodiment, the lower limit of the current time setting range can be set to 95% of the current time setting value of the oxygen concentration, and the upper limit of the current time setting range can be set to 105% of the current time setting value of the oxygen concentration.
[0088] When the detected oxygen concentration in the material in the normoxic zone 2 is lower than 95% of the current time setting value of the calculated oxygen concentration in the material in the normoxic zone 2, the aeration device is controlled to increase the aeration amount. When the detected oxygen concentration in the material in the normoxic zone 2 is higher than 105% of the current time setting value of the calculated oxygen concentration in the material in the normoxic zone 2, the aeration device is controlled to decrease the aeration amount or stop aeration. When the detected oxygen concentration in the material in the normoxic zone 2 is higher than 95% of the current time setting value of the calculated oxygen concentration in the material in the normoxic zone 2 and lower than 105% of the current time setting value of the calculated oxygen concentration in the material in the normoxic zone 2, the aeration amount of the aeration device is not changed.
[0089] In the embodiment of the present application, when the aeration amount of the low-oxygen zone 1 and the super-low-oxygen zone 3 is controlled, the oxygen concentration setting range needs to be set for the low-oxygen zone 1 and the super-low-oxygen zone 3 respectively.
[0090] The low-oxygen zone oxygen concentration sensor 17 detects the oxygen concentration in the material in the low-oxygen zone 1 in real time, and the control device controls the aeration device according to the detected oxygen concentration in the material in the low-oxygen zone 1 and the oxygen concentration setting range corresponding to the low-oxygen zone 1. When the detected oxygen concentration in the material in the low-oxygen zone 1 is lower than the lower limit of the oxygen concentration setting range of the low-oxygen zone 1, the aeration device is controlled to increase the aeration amount. When the detected oxygen concentration in the material in the low-oxygen zone 1 is higher than the upper limit of the oxygen concentration setting range of the low-oxygen zone 1, the aeration device is controlled to decrease the aeration amount or stop aeration. When the detected oxygen concentration in the material in the low-oxygen zone 1 is higher than the lower limit of the oxygen concentration setting range of the low-oxygen zone 1 and lower than the upper limit of the oxygen concentration setting range of the low-oxygen zone 1, the aeration amount of the aeration device is not changed.
[0091] Similarly, the oxygen concentration sensor 8 detects the oxygen concentration in the material in the ultra-low oxygen zone 3 in real time, and the control device controls the aeration device according to the detected oxygen concentration in the material in the ultra-low oxygen zone 3 and the oxygen concentration setting range corresponding to the ultra-low oxygen zone 3. When the detected oxygen concentration in the material in the ultra-low oxygen zone 3 is lower than the lower limit of the oxygen concentration setting range of the ultra-low oxygen zone 3, the control device increases the aeration amount. When the detected oxygen concentration in the material in the ultra-low oxygen zone 3 is higher than the upper limit of the oxygen concentration setting range of the ultra-low oxygen zone 3, the control device reduces the aeration amount or stops the aeration. When the detected oxygen concentration in the material in the ultra-low oxygen zone 3 is higher than the lower limit of the oxygen concentration setting range of the ultra-low oxygen zone 3 and lower than the upper limit of the oxygen concentration setting range of the ultra-low oxygen zone 3, the aeration amount of the control device is unchanged.
[0092] In specific embodiments, the oxygen concentration setting range of the material in the low oxygen zone 1 can be 3% to 5%. The oxygen concentration setting range of the material in the ultra-low oxygen zone 3 can be 1% to 3%.
[0093] In the embodiments of the present application, the aeration device includes an aerator 10, an aeration pipeline, and a first connecting pipeline 11.
[0094] The aerator 10 is arranged outside the reactor body. The aeration pipeline is arranged inside the reactor body and located at the bottom of the reactor body. The side wall of the aeration pipeline is provided with aeration holes arranged at intervals. The first connecting pipeline 11 is arranged outside the reactor body, and the first connecting pipeline 11 connects the aeration pipeline and the aerator 10.
[0095] When the aerator 10 is running, it can transport air or oxygen and other gases into the aeration pipeline and transport them into the reactor body through the aeration holes, thereby supplementing oxygen for the normal oxygen zone 2. Arranging the aeration pipeline at the bottom of the reactor body can promote the uniform distribution of oxygen in the material in the normal oxygen zone 2 and significantly improve the ventilation efficiency of the normal oxygen zone 2.
[0096] In the embodiments, the reactor body includes a box body 12, a partition plate assembly, and a separation assembly.
[0097] The inside of the box body 12 has a containing space, the partition plate assembly is arranged at the bottom of the box body 12, and the partition plate assembly has a spacing with the bottom wall of the box body 12 to form an aeration cavity.
[0098] The partition plate assembly is provided with a plurality of communication holes arranged at intervals, and the communication holes can only allow the gas in the aeration cavity to flow upward to the partition plate assembly, and the moisture above the partition plate assembly cannot flow into the aeration cavity. Specifically, the diameter of the communication hole can be controlled to be in the range of 2 to 10 mm.
[0099] To avoid accidental leakage of moisture above the partition plate assembly to the aeration chamber, a cleaning hole with controllable opening and closing state can be provided at the position of the side wall of the tank 12 corresponding to the aeration chamber, so as to periodically clean the aeration chamber. Each aeration chamber corresponds to a cleaning hole.
[0100] The partition assembly is arranged in the aeration chamber, and the partition assembly divides the aeration chamber into a micro-aeration chamber 14, an aerobic aeration chamber 15 and a low-oxygen aeration chamber 16. The micro-aeration chamber 14 is located below the low-oxygen zone 1, the aerobic aeration chamber 15 is located below the normal-oxygen zone 2, and the low-oxygen aeration chamber 16 is located below the super-low-oxygen zone 3.
[0101] Specifically, the partition plate assembly includes a low-oxygen zone partition plate 7, a normal-oxygen zone partition plate 9 and a super-low-oxygen zone partition plate 13. The low-oxygen zone partition plate 7 is located above the micro-aeration chamber 14, and the low-oxygen zone partition plate 7 is detachably connected with the tank 12. The normal-oxygen zone partition plate 9 is located above the aerobic aeration chamber 15, and the normal-oxygen zone partition plate 9 is detachably connected with the tank 12. The super-low-oxygen zone partition plate 13 is located above the low-oxygen aeration chamber 16, and the super-low-oxygen zone partition plate 13 is detachably connected with the tank 12.
[0102] In this way, the partition plate assembly is arranged in blocks and detachably connected with the tank 12, facilitating cleaning of any one of the micro-aeration chamber 14, the aerobic aeration chamber 15 and the low-oxygen aeration chamber 16.
[0103] In specific embodiments, the diameter of the communication hole on the low-oxygen zone partition plate 7 is set to 2-5 mm, and the opening rate of the low-oxygen zone partition plate 7 is controlled within the range of 10%-20%. The diameter of the communication hole on the normal-oxygen zone partition plate 9 is set to 5-10 mm, and the opening rate of the normal-oxygen zone partition plate 9 is controlled within the range of 20%-50%. The diameter of the communication hole on the super-low-oxygen zone partition plate 13 is set to 2-5 mm, and the opening rate of the super-low-oxygen zone partition plate 13 is controlled within the range of 10%-20%.
[0104] The aeration pipeline includes a first aeration pipeline 18, a second aeration pipeline 19 and a third aeration pipeline 20. The first aeration pipeline 18 is arranged in the micro-aeration chamber 14, the second aeration pipeline 19 is arranged in the aerobic aeration chamber 15, and the third aeration pipeline 20 is arranged in the low-oxygen aeration chamber 16. In this way, after the gas enters the corresponding aeration chamber, it can be uniformly distributed in the aeration chamber, and then flow to the reaction zone through the communication hole, increasing the aeration area range of the aeration device in each reaction zone, and the aeration is more uniform. Moreover, direct contact between the aeration pipeline and the material can be avoided, which is beneficial to prolong the service life of the aeration pipeline.
[0105] The first connecting pipeline 11 has three branch pipelines, which are connected with the first aeration pipeline 18, the second aeration pipeline 19 and the third aeration pipeline 20 respectively. The first control valve 21 and the flow meter 22 are arranged on the three branch pipelines, the first control valve 21 can control the on-off state of the branch pipeline and adjust the flow in the branch pipeline.
[0106] The flow meter 22 and the first control valve 21 are electrically connected with the control device 6. The control device 6 can control the aeration amount of each zone separately according to the oxygen demand in the low-oxygen zone 1, the normal-oxygen zone 2 and the ultra-low-oxygen zone 3.
[0107] The partition assembly includes a partition strip 39, the low-oxygen zone 1, the normal-oxygen zone 2 and the ultra-low-oxygen zone 3 are distributed along the longitudinal direction of the reactor body, the partition strip 39 extends along the transverse direction of the reactor body, and the partition strip 39 is sealingly connected to the bottom wall of the box body 12, the side wall of the box body 12 and the partition plate assembly, so that the micro-aerobic aeration cavity 14, the aerobic aeration cavity 15 and the low-oxygen aeration cavity 16 are independent of each other to avoid mutual influence.
[0108] Supporting blocks 40 are further arranged between the partition plate assembly and the bottom wall of the box body 12 to support the partition plate assembly and improve the rigidity of the partition plate assembly. The supporting blocks 40 are arranged in a plurality of intervals.
[0109] The partition plate assembly can be detachably connected with the box body 12, the partition strip 39 and the supporting blocks 40 for later maintenance.
[0110] In the embodiment of the application, the reactor body is internally provided with a stirring device, and a lifting mechanism is arranged between the low-oxygen zone oxygen concentration sensor 17 and the top wall of the reactor body, between the normal-oxygen zone oxygen concentration sensor 4 and the top wall of the reactor body, between the ultra-low-oxygen zone oxygen concentration sensor 8 and the top wall of the reactor body, between the normal-oxygen zone temperature sensor 5 and the top wall of the reactor body, and between the normal-oxygen zone moisture sensor 23 and the top wall of the reactor body. The lifting mechanism can drive any one of the low-oxygen zone oxygen concentration sensor 17, the normal-oxygen zone oxygen concentration sensor 4, the ultra-low-oxygen zone oxygen concentration sensor 8, the normal-oxygen zone temperature sensor 5 and the normal-oxygen zone moisture sensor 23 to lift to adjust the height of any one of the low-oxygen zone oxygen concentration sensor 17, the normal-oxygen zone oxygen concentration sensor 4, the ultra-low-oxygen zone oxygen concentration sensor 8, the normal-oxygen zone temperature sensor 5 and the normal-oxygen zone moisture sensor 23.
[0111] The stirring device and the lifting mechanism are electrically connected with the control device 6. When the stirring device is running, the control device 6 can control the low-oxygen-zone oxygen concentration sensor 17, the normal-oxygen-zone oxygen concentration sensor 4, the ultra-low-oxygen-zone oxygen concentration sensor 8, the normal-oxygen-zone temperature sensor 5 and the normal-oxygen-zone moisture sensor 23 to rise to the top of the reactor body. When the stirring device is stopped, the control device 6 can control the low-oxygen-zone oxygen concentration sensor 17, the normal-oxygen-zone oxygen concentration sensor 4, the ultra-low-oxygen-zone oxygen concentration sensor 8, the normal-oxygen-zone temperature sensor 5 and the normal-oxygen-zone moisture sensor 23 to descend to be immersed in the material.
[0112] In the embodiment, the stirring device comprises a support seat 24, a first driving mechanism, a mounting seat 25, a second driving mechanism, a spiral stirring mechanism 26 and a scraper 28.
[0113] The support seat 24 is movable along the longitudinal direction of the reactor body relative to the reactor body, and the first driving mechanism is used to drive the support seat 24 to move along the longitudinal direction of the reactor body.
[0114] The mounting seat 25 is arranged on the support seat 24, and the support seat 24 can drive the mounting seat 25 to move along the longitudinal direction of the reactor body.
[0115] The mounting seat 25 is movable along the transverse direction of the reactor body relative to the support seat 24. The second driving mechanism is used to drive the mounting seat 25 to move along the transverse direction of the reactor body.
[0116] The spiral stirring mechanism 26 is arranged on the mounting seat 25, and the mounting seat 25 can drive the spiral stirring mechanism 26 to move along the longitudinal direction of the reactor body and also can drive the spiral stirring mechanism 26 to move along the transverse direction of the reactor body.
[0117] The spiral stirring shaft 27 of the spiral stirring mechanism 26 is rotatable about its own axis relative to the mounting seat 25. Through the rotation of the spiral stirring shaft 27, the material can be stirred. The spiral stirring shaft 27 is arranged obliquely relative to the bottom wall of the reactor body. By controlling the rotation direction of the spiral stirring shaft 27, the material can be moved in the direction from the low-oxygen zone 1 to the ultra-low-oxygen zone 3, so as to realize continuous composting.
[0118] The spiral stirring mechanism 26 has the functions of stirring and longitudinal conveying at the same time, and does not need to additionally arrange a longitudinal conveying device for the material, which is favorable for simplifying the structure of the reactor, reducing the floor area and reducing energy consumption.
[0119] The scraper 28 is located below the spiral stirring shaft 27. The scraper 28 is fixed relative to the mounting seat 25. When the mounting seat 25 moves along the longitudinal direction of the reactor body, the scraper 28 is used to scrape the material on the bottom wall of the low-oxygen zone 1, the bottom wall of the normal-oxygen-zone 2 and the bottom wall of the ultra-low-oxygen-zone 3, so as to reduce the accumulation of the material on the bottom of the reactor body and improve the conveying efficiency.
[0120] The scraper 28 interacts with the partition plate assembly, the aeration pipeline is arranged below the partition plate assembly, interference of the aeration pipeline on the scraper 28 can be avoided, wear of the aeration pipeline can be avoided, durability is improved, and service life is prolonged.
[0121] Specifically, the spiral stirring shaft 27 can be arranged as a hollow shaft, and the scraper 28 has a connecting shaft which is arranged in the hollow shaft and is fixedly connected with the mounting seat 25.
[0122] The first driving mechanism, the second driving mechanism and the spiral stirring mechanism 26 are electrically connected with the control device 6, the control device 6 can control the position and start-stop of the spiral stirring mechanism 26 as required, and automatic control is realized.
[0123] In specific embodiments, the height of the end of the spiral stirring shaft 27 close to the ultra-low oxygen zone 3 is greater than the height of the other end, and the end wall of the end where the discharge port of the box body 12 is located is also arranged to be inclined, and the inclination angle of the end wall of the end where the discharge port of the box body 12 is located is consistent with the inclination angle of the spiral stirring shaft 27. The end wall of the end where the discharge port of the box body 12 is located is close to the spiral stirring shaft 27, and the material in the ultra-low oxygen zone 3 can be transported to the discharge port through the rotation of the spiral stirring shaft 27, so that the material is discharged from the discharge port.
[0124] The inclination angle of the spiral stirring shaft 27 can be controlled within the range of 10°~20°, and specifically, the inclination angle of the spiral stirring shaft 27 can be set to 15°.
[0125] It should be noted that the discharge port is provided with a sealing plate, and in a natural state, the sealing plate closes the discharge port. When the spiral stirring shaft 27 transports the material to the discharge port, the material exerts a pressing force on the sealing plate, so that the sealing plate can be rotated to open the discharge port.
[0126] In the embodiment, the stirring device further comprises a stirring oxygen concentration sensor, which is arranged on the spiral stirring mechanism 26. The stirring oxygen concentration sensor is used to detect the oxygen concentration in the material around the spiral stirring mechanism 26 in real time when the stirring device is running, so as to determine the region where the spiral stirring mechanism 26 is located according to the detected oxygen concentration in the material around the spiral stirring mechanism 26, and then control the rotating speed of the spiral stirring mechanism 26.
[0127] For different regions in the low-oxygen zone 1, the normal-oxygen zone 2 and the ultra-low-oxygen zone 3, the rotating speed of the spiral stirring mechanism is different. When the spiral stirring mechanism 26 is in the low-oxygen zone 1, the spiral stirring mechanism 26 is controlled to rotate 10~20 times per minute; when the spiral stirring mechanism 26 is in the normal-oxygen zone 2, the spiral stirring mechanism 26 is controlled to rotate 20~30 times per minute; and when the spiral stirring mechanism 26 is in the ultra-low-oxygen zone 3, the spiral stirring mechanism 26 is controlled to rotate 5~10 times per minute.
[0128] The self-propelled precise cooperative control intelligent composting reactor provided by the embodiment of the present application enables the spiral stirring mechanism 26 to run once from the direction of the charging port to the discharging port of the reactor body, and can push the material in the reactor body to move in the direction from the low-oxygen zone to the ultra-low-oxygen zone. Specifically, the spiral stirring mechanism 26 can be operated once a day.
[0129] In the embodiment, first support guide mechanisms are respectively arranged between the two ends of the transverse direction of the support seat 24 and the reactor body, and the first support guide mechanism comprises a first guide groove 29 and a first roller 30.
[0130] The first guide groove 29 is arranged on the reactor body, and the first guide groove 29 extends along the longitudinal direction of the reactor body. The first roller 30 is rotatably arranged on the support seat 24, and the rolling axis of the first roller 30 relative to the support seat 24 is arranged along the transverse direction of the reactor body, and the first roller 30 can roll in the first guide groove 29. Through the cooperation of the first roller 30 and the first guide groove 29, the sliding of the support seat 24 can be guided.
[0131] The first driving mechanism comprises a first rack 31, a first gear 32 and a first driving member 37.
[0132] The first rack 31 is arranged on the reactor body, and the first rack 31 extends along the longitudinal direction of the reactor body. The first gear 32 is in meshing transmission with the first rack 31, the first gear 32 is rotatably arranged on the support seat 24, and the axis of the first gear 32 is arranged along the vertical direction of the reactor body. The first driving member 37 is arranged on the support seat 24, the first driving member 37 is in transmission connection with the first gear 32, and the first driving member 37 is electrically connected with the control device 6.
[0133] The bottom wall of the first guide groove 29 supports the first roller 30, which can bear the load, avoiding the influence of gravity and the like on the first gear 32 and the first rack 31. The meshing transmission of the first gear 32 and the first rack 31 is not affected by the gravity of the support seat 24, the mounting seat 25, the spiral stirring mechanism 26 and the like, which reduces the load of the first rack 31 and the first driving member 37, is beneficial to the miniaturization of the first driving member 37, reduces the mass of the first driving member 37, further reduces the load of the support seat 24, reduces the energy consumption, and reduces the deformation of the support seat 24 and the first rack 31.
[0134] Similarly, second support guide mechanisms are arranged between the two ends of the longitudinal direction of the mounting seat 25 and the support seat 24, and the second support guide mechanism comprises a second guide groove 33 and a second roller 34.
[0135] The second guide groove 33 is arranged on the support base 24 and extends along the lateral direction of the reactor body.
[0136] The second driving mechanism comprises a second rack 35, a second gear 36 and a second driving member 38.
[0137] The second rack 35 is arranged on the support base 24 and extends along the lateral direction of the reactor body. The second gear 36 is in meshing transmission with the second rack 35. The second gear 36 is rotatably arranged on the mounting base 25, and the axis of the second gear 36 extends along the vertical direction of the reactor body. The second driving member 38 is arranged on the mounting base 25 and is in transmission connection with the second gear 36. The second driving member 38 is electrically connected with the control device 6.
[0138] The bottom wall of the second guide groove 33 supports the second roller 34 and can bear the load, thereby avoiding the influence of gravity on the second gear 36 and the second rack 35. The meshing transmission between the second gear 36 and the second rack 35 is not affected by the gravity of the mounting base 25 and the spiral stirring mechanism 26. The load of the second rack 35 and the second driving member 38 is reduced, which is conducive to the miniaturization of the second driving member 38, reduces the mass of the second driving member 38, further reduces the load of the mounting base 25, reduces the energy consumption, and reduces the deformation of the mounting base 25 and the second rack 35.
[0139] In the embodiment, the self-propelled precise cooperative control intelligent composting reactor further comprises a feeding device, which is used for adding materials to the material inlet of the reactor body.
[0140] The feeding device comprises a guide bracket 42, a connecting bracket 43, a material conveying device 41 and a third driving mechanism.
[0141] The guide bracket 42 comprises a vertical bracket and an arc-shaped bracket. The vertical bracket extends along the vertical direction of the reactor body. The first end of the arc-shaped bracket is tangentially connected to the upper end of the vertical bracket. The second end of the arc-shaped bracket is connected to the reactor body, and the tangent line of the second end of the arc-shaped bracket is parallel to the longitudinal direction of the reactor body. For details, refer to Figure 8 .
[0142] The connecting bracket 43 can reciprocally slide along the guide bracket 42. The third driving mechanism is used for driving the connecting bracket 43 to reciprocally slide relative to the guide bracket 42. The third driving mechanism is electrically connected with the control device 6.
[0143] The feeding device 41 is used for transporting materials between the material source and the reactor body, and can be a trolley.
[0144] The feeding device 41 is detachably connected with the connecting bracket 43. After the feeding device 41 is disconnected with the connecting bracket 43, the feeding device 41 can move reciprocally between the reactor body and the material source to transport materials. When the feeding device 41 transports materials to the reactor body, the feeding device 41 is connected with the connecting bracket 43, and the third driving mechanism is controlled to operate, so as to drive the feeding device 41 to ascend along the guide bracket 42 to gradually approach the charging port of the reactor body.
[0145] One end of the feeding device 41 is open, and the open end of the feeding device 41 is arranged upward when the connecting bracket 43 is located on the vertical bracket. Correspondingly, when the connecting bracket 43 is located on the second end of the arc-shaped bracket, the plane where the open end of the feeding device 41 is located is perpendicular to the longitudinal direction of the reactor body. At this time, the materials in the feeding device 41 can be unloaded by themselves.
[0146] A sealing plate is arranged at the charging port, and the sealing plate seals the charging port in a natural state. When the materials in the feeding device 41 are unloaded, the materials can press the sealing plate to rotate to open the charging port.
[0147] For the detachable connection between the connecting bracket 43 and the feeding device 41, a slot can be arranged on each of the opposite sides of the feeding device 41, and a pair of fork arms can be arranged on the connecting bracket 43 and can be inserted into the slots. When the fork arms are inserted into the slots, the feeding device 41 and the connecting bracket 43 are connected together, and the connecting bracket 43 can drive the feeding device 41 to ascend and descend. When it is needed to disconnect the feeding device 41 from the connecting bracket 43, the fork arms can be moved out of the slots.
[0148] The third driving mechanism includes a chain wheel 44, a chain 45 and a third driving member. The chain wheel 44 is arranged at the upper end of the guide bracket 42, and the third driving member can drive the chain wheel 44 to rotate. The chain 45 is arranged around the chain wheel 44, the first end of the chain 45 is connected with the connecting bracket 43, and the second end of the chain 45 is arranged in suspension. The third driving member drives the chain wheel 44 to rotate, so as to drive the first end of the chain 45 to ascend and descend, thereby driving the connecting bracket 43 to ascend and descend.
[0149] To ensure the stability and reliability of the third driving mechanism and prevent the chain 45 from being disconnected from the chain wheel 44, a counterweight can be arranged at the second end of the chain 45 to ensure the reliable engagement between the chain 45 and the chain wheel 44.
[0150] The above-mentioned first driving member 37, second driving member 38 and third driving member can be motors, but are not limited to motors. When motors are used, a speed reducer can be adapted.
[0151] In summary, the self-moving precision cooperative regulation intelligent composting reactor provided by the embodiments of the present application realizes real-time automatic control of aeration and stirring and the like, reduces the requirement for professional skills of an operator and labor intensity of personnel, improves composting efficiency, guarantees the quality of a composting product, and reduces operating energy consumption. Meanwhile, a fault diagnosis and alarm function can be provided to discover and prompt abnormal conditions in operation in a timely manner.
[0152] Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present application, but not to limit them; although the present application has been described in detail with reference to the foregoing embodiments, those skilled in the art should understand that: it can still modify the technical solutions recorded in the foregoing embodiments, or make equivalent replacement for part of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the spirit and scope of the technical solutions of the embodiments of the present application.
Claims
1. A self-propelled precision synergistic control intelligent compost reactor, characterized in that, The reactor body has a low-oxygen zone (1), a normal-oxygen zone (2) and a super-low-oxygen zone (3) arranged in sequence inside, the low-oxygen zone (1) and the super-low-oxygen zone (3) are communicated with the normal-oxygen zone (2), the reactor body comprises a box (12), a partition plate assembly and a partition assembly, the box (12) has an accommodating space inside, the partition plate assembly is arranged at the bottom of the box (12), there is a spacing between the partition plate assembly and the bottom wall of the box (12) to form an aeration cavity, a plurality of spaced communication holes are arranged on the partition plate assembly, the communication holes are arranged to be adapted only for the gas in the aeration cavity to flow upwards to the partition plate assembly, the partition assembly is arranged in the aeration cavity, and the partition assembly is adapted to divide the aeration cavity into a micro-oxygen aeration cavity (14), an aerobic aeration cavity (15) and a low-oxygen aeration cavity (16), the micro-oxygen aeration cavity (14) is located below the low-oxygen zone (1), the aerobic aeration cavity (15) is located below the normal-oxygen zone (2), and the low-oxygen aeration cavity (16) is located below the super-low-oxygen zone (3); The aeration device is adapted to aerate the materials in the low-oxygen zone (1), the normal-oxygen zone (2) and the super-low-oxygen zone (3) respectively, and comprises an aerator (10), an aeration pipeline and a first connecting pipeline (11), the aerator (10) is arranged outside the reactor body, the aeration pipeline is arranged inside the reactor body and at the bottom of the reactor body, the side wall of the aeration pipeline is provided with spaced aeration holes, the first connecting pipeline (11) is arranged outside the reactor body, the first connecting pipeline (11) connects the aeration pipeline and the aerator (10), the aeration pipeline comprises a first aeration pipeline (18), a second aeration pipeline (19) and a third aeration pipeline (20), the first aeration pipeline (18) is arranged in the micro-oxygen aeration cavity (14), the second aeration pipeline (19) is arranged in the aerobic aeration cavity (15), the third aeration pipeline (20) is arranged in the low-oxygen aeration cavity (16), the first connecting pipeline (11) has three branch pipelines, the three branch pipelines are connected with the first aeration pipeline (18), the second aeration pipeline (19) and the third aeration pipeline (20) respectively, and the first control valve (21) and the flow meter (22) are arranged on the three branch pipelines, the first control valve (21) is adapted to control the on-off state of the branch pipeline and adjust the flow in the branch pipeline. The oxygen concentration sensor comprises a low-oxygen-zone oxygen concentration sensor (17) adapted to detect the oxygen concentration in the material in the low-oxygen zone (1), a normal-oxygen-zone oxygen concentration sensor (4) adapted to detect the oxygen concentration in the material in the normal-oxygen zone (2), and a super-low-oxygen-zone oxygen concentration sensor (8) adapted to detect the oxygen concentration in the material in the super-low-oxygen zone (3); a normal-oxygen-zone temperature sensor (5) adapted to detect the temperature of the material in the normal-oxygen zone (2); a normal-oxygen-zone moisture sensor (23) adapted to detect the moisture content of the material in the normal-oxygen zone (2); a control device (6), the aeration device, the low-oxygen-zone oxygen concentration sensor (17), the normal-oxygen-zone oxygen concentration sensor (4), the super-low-oxygen-zone oxygen concentration sensor (8), the normal-oxygen-zone temperature sensor (5), the normal-oxygen-zone moisture sensor (23), the flow meter (22), and the first control valve (21) are electrically connected to the control device (6), the control device (6) is adapted to determine the current-time set value of the oxygen concentration in the material in the normal-oxygen zone (2) according to the current-time temperature of the material in the normal-oxygen zone (2) and the current-time moisture content of the material in the normal-oxygen zone (2), and control the aeration device according to the current-time set value of the oxygen concentration and the current-time oxygen concentration of the material in the normal-oxygen zone (2).
2. The self-propelled precision co-regulatory intelligent compost reactor according to claim 1, characterized in that, The relationship among the current-time temperature of the material in the normal-oxygen zone (2), the current-time moisture content of the material in the normal-oxygen zone (2), and the current-time set value of the oxygen concentration in the material in the normal-oxygen zone (2) is C1=a×WC-b×T1+e, wherein C1 is the current-time set value of the oxygen concentration in the material in the normal-oxygen zone (2), WC is the current-time moisture content of the material in the normal-oxygen zone (2), T1 is the current-time temperature of the material in the normal-oxygen zone (2), and a, b, and e are constants; The control device is further adapted to determine the current-time set range of the oxygen concentration according to the current-time set value of the oxygen concentration, and control the aeration device according to the current-time set range of the oxygen concentration, the lower limit value of the current-time set range being 95% of the current-time set value of the oxygen concentration, and the upper limit value of the current-time set range being 105% of the current-time set value of the oxygen concentration.
3. The self-propelled precision co-regulatory intelligent compost reactor according to claim 1, characterized in that, The control device (6) is further adapted to control the aeration device according to the oxygen concentration in the material in the low-oxygen zone (1) and the set range of the oxygen concentration in the material in the low-oxygen zone (1), the set range of the oxygen concentration in the material in the low-oxygen zone (1) being 3% to 5%. The control device (6) is also adapted to control the aeration device according to the oxygen concentration in the material in the ultra-low oxygen zone (3) and the set range of the oxygen concentration in the material in the ultra-low oxygen zone (3), the set range of the oxygen concentration in the material in the ultra-low oxygen zone (3) being 1% to 3%.
4. The self-propelled precision co-regulatory intelligent compost reactor according to claim 1, characterized in that, The partition plate assembly comprises: A low-oxygen-zone partition plate (7) is located above the micro-aerobic aeration cavity (14), the low-oxygen-zone partition plate (7) is detachably connected with the box body (12), the diameter of the communication hole on the low-oxygen-zone partition plate (7) is 2 to 5 millimeters, and the opening rate of the low-oxygen-zone partition plate (7) is 10% to 20%; An aerobic-zone partition plate (9) is located above the aerobic aeration cavity (15), the aerobic-zone partition plate (9) is detachably connected with the box body (12), the diameter of the communication hole on the aerobic-zone partition plate (9) is 5 to 10 millimeters, and the opening rate of the aerobic-zone partition plate (9) is 20% to 50%; An ultra-low-oxygen-zone partition plate (13) is located above the low-oxygen aeration cavity (16), the ultra-low-oxygen-zone partition plate (13) is detachably connected with the box body (12), the diameter of the communication hole on the ultra-low-oxygen-zone partition plate (13) is 2 to 5 millimeters, and the opening rate of the ultra-low-oxygen-zone partition plate (13) is 10% to 20%.
5. The self-propelled precision co-regulatory intelligent compost reactor according to claim 1, characterized in that, The reactor body is internally provided with a stirring device, and a lifting mechanism is arranged between the low-oxygen-zone oxygen concentration sensor (17) and the top wall of the reactor body, between the aerobic-zone oxygen concentration sensor (4) and the top wall of the reactor body, between the ultra-low-oxygen-zone oxygen concentration sensor (8) and the top wall of the reactor body, between the aerobic-zone temperature sensor (5) and the top wall of the reactor body, and between the aerobic-zone moisture sensor (23) and the top wall of the reactor body; The stirring device and the lifting mechanism are electrically connected with the control device (6), and the control device (6) is adapted to control the low-oxygen-zone oxygen concentration sensor (17), the aerobic-zone oxygen concentration sensor (4), the ultra-low-oxygen-zone oxygen concentration sensor (8), the aerobic-zone temperature sensor (5), and the aerobic-zone moisture sensor (23) to rise to the top of the reactor body when the stirring device is running, and to control the low-oxygen-zone oxygen concentration sensor (17), the aerobic-zone oxygen concentration sensor (4), the ultra-low-oxygen-zone oxygen concentration sensor (8), the aerobic-zone temperature sensor (5), and the aerobic-zone moisture sensor (23) to descend to be immersed in the material when the stirring device stops running.
6. The self-propelled precision co-regulatory intelligent compost reactor according to claim 5, characterized in that, The stirring device comprises: A support seat (24) is adapted to move along the longitudinal direction of the reactor body relative to the reactor body; A first driving mechanism is adapted to drive the support seat (24) to move along the longitudinal direction of the reactor body, and the first driving mechanism is electrically connected with the control device (6); A mounting seat (25) is arranged on the support seat (24), and the mounting seat (25) is adapted to move along the transverse direction of the reactor body relative to the support seat (24); A second driving mechanism is adapted to drive the mounting seat (25) to move along the transverse direction of the reactor body, and the second driving mechanism is electrically connected with the control device (6); A spiral stirring mechanism (26) is arranged on the mounting seat (25), a spiral stirring shaft (27) of the spiral stirring mechanism (26) is adapted to rotate around its own axis relative to the mounting seat (25), the spiral stirring shaft (27) is arranged obliquely relative to the bottom wall of the reactor body, and the spiral stirring mechanism (26) is electrically connected with the control device (6); A scraper (28) is arranged below the spiral stirring shaft (27), the scraper (28) is fixed relative to the mounting seat (25), and the scraper (28) is adapted to scrape the materials on the bottom wall of the low-oxygen zone (1), the bottom wall of the normal-oxygen zone (2) and the bottom wall of the ultra-low-oxygen zone (3).
7. The self-propelled precision co-regulatory intelligent compost reactor according to claim 6, characterized in that, The stirring device further comprises: A stirring oxygen concentration sensor is arranged on the spiral stirring mechanism (26), the stirring oxygen concentration sensor is adapted to detect the oxygen concentration in the materials around the spiral stirring mechanism (26) in real time when the stirring device is running, so as to determine the region where the spiral stirring mechanism (26) is located, and then control the rotating speed of the spiral stirring mechanism (26); When the spiral stirring mechanism (26) is in the low-oxygen zone (1), the rotating speed of the spiral stirring mechanism (26) is controlled to be 10-20 revolutions per minute; when the spiral stirring mechanism (26) is in the normal-oxygen zone (2), the rotating speed of the spiral stirring mechanism (26) is controlled to be 20-30 revolutions per minute; and when the spiral stirring mechanism (26) is in the ultra-low-oxygen zone (3), the rotating speed of the spiral stirring mechanism (26) is controlled to be 5-10 revolutions per minute.
8. The self-propelled precision co-regulatory intelligent compost reactor according to claim 6, characterized in that, First support guide mechanisms are respectively arranged between the two ends of the transverse direction of the support seat (24) and the reactor body, and each first support guide mechanism comprises: A first guide groove (29) is arranged on the reactor body, and the first guide groove (29) extends along the longitudinal direction of the reactor body; A first roller (30) is rotatably arranged on the support seat (24), a rolling axis of the first roller (30) is arranged along the transverse direction of the reactor body relative to the support seat (24), and the first roller (30) is adapted to roll in the first guide groove (29); The first driving mechanism comprises: A first rack (31) is arranged on the reactor body, and the first rack (31) extends along the longitudinal direction of the reactor body; A first gear (32) is in meshing transmission with the first rack (31), and the first gear (32) is rotatably arranged on the support seat (24), and an axis of the first gear (32) is arranged along the vertical direction of the reactor body; A first driving member (37) is arranged on the support base (24), the first driving member (37) is in transmission connection with the first gear (32), and the first driving member (37) is in electrical connection with the control device (6).
9. The self-propelled precision co-regulatory intelligent compost reactor according to claim 6, characterized in that, Second support guide mechanisms are arranged between the longitudinal two ends of the mounting base (25) and the support base (24), and the second support guide mechanisms comprise: A second guide groove (33) is arranged on the support base (24), and the second guide groove (33) extends along the lateral direction of the reactor body; A second roller (34) is rotatably arranged on the mounting base (25), the rolling axis of the second roller (34) relative to the mounting base (25) is arranged along the longitudinal direction of the reactor body, and the second roller (34) is adapted to roll in the second guide groove (33); The second driving mechanism comprises: A second rack (35) is arranged on the support base (24), and the second rack (35) extends along the lateral direction of the reactor body; A second gear (36) is in meshing transmission with the second rack (35), the second gear (36) is rotatably arranged on the mounting base (25), and the axis of the second gear (36) is arranged along the vertical direction of the reactor body; A second driving member (38) is arranged on the mounting base (25), the second driving member (38) is in transmission connection with the second gear (36), and the second driving member (38) is in electrical connection with the control device (6).
Citation Information
Patent Citations
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