Low temperature infrared radiation coupled biological reaction method and device
By coupling biomass with infrared radiation and using infrared irradiation and controlling air rate, the problem of low heating efficiency in traditional biomass treatment is solved, and the microbial reaction efficiency and combustion value are improved.
Patent Information
- Application Number
- CN201811081363.7
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2018-09-17
- Publication Date
- 2024-12-10
- Estimated Expiration
- 2038-09-17
AI Technical Summary
In the existing biomass treatment technology, thermal aeration and heat conduction heating methods have problems such as high energy consumption, difficulty in uniform transmission of temperature and poor insulation performance, resulting in low microbial reaction efficiency and reaction temperature not meeting expectations.
Using low-temperature infrared radiation coupled biological reaction method, the biomass and infrared radiation are coupled, and through infrared irradiation devices and air rate control, non-contact heat transfer and heat radiation transfer are realized, the material temperature is maintained within the appropriate range, and microorganisms are promoted. Aerobic fermentation.
It improves the microbial reactivity and efficiency, shortens the reaction cycle, reduces the moisture content of biomass materials, and increases the combustion value.
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Figure CN109078968B_ABST
Abstract
Description
Technical Field
[0001] The invention relates to a low-temperature infrared radiation coupled biological reaction method and a device thereof, belonging to the field of biomass waste resource processing. Background Art
[0002] Aerobic biological treatment refers to a treatment method that uses aerobic microorganisms (including facultative microorganisms) to metabolize organic matter in the presence of oxygen to stabilize and render it harmless. Microorganisms use existing organic pollutants as substrates for aerobic metabolism, and after a series of biochemical reactions, they release energy step by step, and eventually stabilize as low-energy inorganic matter, achieving the requirement of harmlessness, so that they can be returned to the natural environment or further treated.
[0003] At present, the main heating methods used are thermal aeration and heat conduction. The heat conduction heating rate has a slow response, and the temperature is difficult to be directly transmitted to the center point, which has high energy consumption and poor thermal insulation performance, which greatly increases the heat dissipation. Thermal aeration uses hot air to pass through the biomass pile for direct contact heating. The moment the hot air contacts the biomass material, the surface water vapor will evaporate, directly reducing the temperature of the biomass material, thereby taking most of the heat out of the system, so that the entire reaction temperature cannot reach the expected temperature, affecting the experimental effect. Summary of the invention
[0004] In view of the shortcomings and deficiencies of the prior art, the purpose of the present invention is to provide a low-temperature infrared radiation coupled biological reaction method and a device thereof, which couples the traditional biomass passage for microbial aerobic reaction with infrared radiation, changes the heat transfer from contact to non-contact, and changes the thermal aeration that maintains the material temperature by heat convection heat transfer to thermal radiation, which greatly improves the problem that the hot air quickly passes through the biomass surface, instantly taking away a large amount of water vapor from the biomass surface, and the water evaporation absorbs heat, so that the actual material temperature cannot reach the ideal temperature, optimizes the entire microbial reaction process, greatly improves the microbial reaction activity, further shortens the reaction cycle, and improves the reaction efficiency.
[0005] In order to achieve the above object, the present invention provides a low-temperature infrared radiation coupled biological reaction method, the steps are as follows:
[0006] The biomass material is naturally piled up or placed in a stirring device, and infrared irradiated by an infrared irradiation device. Under the action of heat generation by microbial fermentation, the temperature of the material is further controlled by controlling the power of the infrared irradiation device and the rate of air introduction, so as to provide a stable and suitable environmental temperature for aerobic fermentation and heat generation of microorganisms in the biomass. By turning the pile or mechanical stirring, the temperature of the entire material is promoted to be uniform to ensure the efficient progress of the entire microbial reaction. After the reaction is completed, the material is emptied in time, discharged, and new biomass material is filled in, and the above operation is repeated to realize continuous operation of the process.
[0007] Furthermore, the air introduced is room temperature air, which can provide oxygen for the microbial reaction and provide rapid heat dissipation when the material temperature is too high (higher than the maximum temperature suitable for microbial survival), ensuring that the material temperature is maintained within a suitable ambient temperature range, providing a stable and suitable ambient temperature for the aerobic fermentation heat production of microorganisms in the biomass.
[0008] Furthermore, the biomass materials include organic matter such as straw, feces, domestic garbage, and kitchen waste, but are not limited to the above.
[0009] Furthermore, the temperature of the material is further controlled by controlling the power of the infrared irradiation device and the rate of air introduction, so as to provide a stable and suitable environmental temperature for the aerobic fermentation heat production of microorganisms in the biomass, which can be specifically:
[0010] When the material temperature is lower than the minimum temperature suitable for the survival of microorganisms, increase the power of the infrared irradiation device, or reduce the rate of air introduction, or increase the power of the infrared irradiation device and reduce the rate of air introduction at the same time, so that the material temperature is maintained within the appropriate ambient temperature range;
[0011] When the material temperature is higher than the maximum temperature suitable for the survival of microorganisms, the air supply rate is increased, or the infrared irradiation power is reduced, or the air supply rate is increased and the power of the infrared irradiation device is reduced at the same time, so that the material temperature is maintained within the appropriate ambient temperature range.
[0012] Furthermore, the reaction time is 24-72 hours.
[0013] The present invention also provides a low-temperature infrared radiation coupled bioreactor device, comprising: a reactor and an infrared irradiation device and a stirring device arranged inside the reactor from top to bottom, integrating feeding, discharging, material mixing and reaction in one, the upper cover plate of the reactor is located above the lower box body, and a condensate collection tank and an infrared irradiation device are arranged on the inner wall of the upper cover plate of the reactor from top to bottom, a feed port and an air outlet are arranged between the top of the upper cover plate and the condensate collection tank, and the feed port and the air outlet are located on both sides of the upper cover plate; a liquid outlet, an air inlet and a material outlet are arranged at the bottom of the lower box body of the reactor, the air inlet is located at the center of the bottom of the lower box body, and the liquid outlet and the material outlet are located on both sides of the air inlet.
[0014] The biomass material enters the reactor through the feed port at the upper end of the reactor, is heated by the infrared irradiation device, and is evenly mixed by the stirring device, and a biological reaction occurs. After the reaction is completed, the material is discharged from the discharge port at the lower end of the reactor.
[0015] The infrared irradiation device is used to provide infrared irradiation to the materials in the reaction kettle.
[0016] Furthermore, the infrared irradiation device is an infrared irradiation lamp.
[0017] Furthermore, the infrared irradiation device is symmetrically arranged on the inner wall of the upper cover plate, and the condensed water collecting tank is symmetrically arranged on the inner wall of the upper cover plate, and the condensed water collecting tank is located above the infrared irradiation device.
[0018] The stirring device is a prior art in the art, preferably a double-shaft stirring device, which is used to mix the biomass materials to make them uniformly mixed. For example, a double-screw compost turning shaft includes a forward screw compost turning shaft and a reverse screw compost turning shaft, wherein the forward screw compost turning shaft and the reverse screw compost turning shaft are controlled by a driving motor to realize synchronous operation, and the forward screw compost turning shaft and the reverse screw compost turning shaft rotate in opposite directions.
[0019] Furthermore, the lower box of the reactor has a compost turning plate structure, which is a prior art in the art. A compost turning plate is provided at the end of one end of the twin-screw compost turning shaft to facilitate the reciprocating movement of materials in the two grooves, so that the reaction is more complete and the materials are mixed more evenly.
[0020] Furthermore, the pile turning plate is an arc-shaped structure.
[0021] Furthermore, the cross section of the upper cover of the reactor is a triangular structure, and the condensed water formed on the inner wall surface of the upper cover can flow down freely. The condensed water collecting tank above the infrared irradiation device is used to collect the condensed water generated during the process.
[0022] Furthermore, the air inlet at the lower end of the reactor is connected to a low-temperature aeration tank for introducing air into the reactor to provide oxygen for microbial reaction. Ventilation and oxygenation avoid anaerobic reaction, so as to maximize the oxidation function of the material.
[0023] Furthermore, a thermocouple for online temperature collection in the reactor is provided in the reactor, and the thermocouple is connected to a temperature controller, an infrared irradiation device, and a low-temperature aeration tank. The temperature of the material is controlled by controlling the power of the infrared irradiation device and the rate of air introduction, thereby providing a stable and suitable ambient temperature for aerobic fermentation heat production by microorganisms in the biomass.
[0024] Furthermore, the temperature controller is a temperature controller.
[0025] Furthermore, the discharge port at the lower end of the reactor is connected to a solid waste treatment unit, and the material discharged from the reactor enters the solid waste treatment unit for solid waste treatment.
[0026] Furthermore, the gas outlet at the upper end of the reactor is connected to a waste gas treatment unit, and the discharged reactor gas enters the waste gas treatment unit for waste gas treatment.
[0027] Furthermore, the gas outlet is a water vapor duct.
[0028] Furthermore, the liquid outlet at the lower end of the reactor is connected to a waste liquid treatment unit, and the liquid discharged from the reactor enters the waste liquid treatment unit for waste liquid treatment.
[0029] The low-temperature aeration tank, solid waste treatment unit, waste gas treatment unit, and waste liquid treatment unit are all existing technologies in the field, and technicians in the field can select or combine them according to actual conditions.
[0030] The above-mentioned method for treating biomass waste by using a low-temperature infrared radiation coupled bioreactor comprises the following steps:
[0031] The biomass material enters the reactor through the feed port at the upper end of the reactor, the material is irradiated and heated by the infrared irradiation device above the material, the material is evenly mixed by the stirring device, and air is introduced into the reactor through the low-temperature aeration tank to provide oxygen for the microbial reaction. The material after the reaction is discharged from the discharge port at the lower end of the reactor, and new biomass material is filled in. The above operation is repeated to realize continuous operation of the process.
[0032] Under the action of heat production by microbial fermentation, the temperature of the material is further controlled by controlling the power of the infrared irradiation device and the rate of air introduction, providing a stable and suitable ambient temperature for the aerobic fermentation heat production of microorganisms in the biomass. Mechanical stirring is performed regularly every day to promote the uniformity of the temperature of the entire material to ensure the efficient progress of the entire microbial reaction.
[0033] The gas generated after the reaction is drawn out of the reactor through the induced draft fan and enters the exhaust gas treatment unit through the steam channel for exhaust gas treatment. The condensed water generated by the reaction is collected through the condensed water collection tank, and the liquid generated after the reaction is discharged from the liquid outlet at the lower end of the reactor for residual liquid treatment.
[0034] Compared with the prior art, the present invention has the following beneficial effects:
[0035] 1. The traditional biomass is coupled with microbial aerobic reaction and infrared irradiation, changing the heat transfer from contact to non-contact, and changing the thermal aeration that maintains the material temperature by convection heat transfer to thermal radiation, which greatly improves the problem that the hot air quickly passes through the biomass surface, instantly taking away a large amount of water vapor from the biomass surface, and the water evaporation absorbs heat, so that the actual material temperature cannot reach the ideal temperature.
[0036] 2. Optimized the entire microbial reaction process, greatly improved the microbial reaction activity, further shortened the reaction cycle, and improved the reaction efficiency.
[0037] 3. After the entire microbial reaction process, the moisture content of the biomass material is reduced to half of the original, and the combustion value is improved. BRIEF DESCRIPTION OF THE DRAWINGS
[0038] Figure 1 This is a schematic diagram of low-temperature infrared radiation coupled biological reaction technology.
[0039] Figure 2 It is a schematic diagram of the structure of the reactor in the low-temperature infrared radiation coupled bioreactor.
[0040] Figure 3 It is a system flow chart of low-temperature infrared radiation coupled biological reaction device.
[0041] In the figure: 1. forward screw device, 2. reverse screw device, 3. compost turning plate, 4. infrared irradiation device, 5. condensate collecting tank, 6. upper cover plate, 7. lower box, 8. reactor, 9. feed port, 10. discharge port, 11. air inlet, 12. air outlet, 13. liquid outlet, 14. low-temperature aeration tank, 15. solid waste treatment unit, 16. waste gas treatment unit, 17. waste liquid treatment unit, 18. materials. DETAILED DESCRIPTION
[0042] The following non-limiting embodiments may enable a person skilled in the art to more fully understand the present invention, but are not intended to limit the present invention in any way.
[0043] In the description of the present invention, it is necessary to understand that the directions or positional relationships indicated by directional words such as "front, back, up, down, left, right", "lateral, vertical, perpendicular, horizontal" and "top, bottom" are usually based on the directions or positional relationships shown in the drawings. They are only for the convenience of describing the present invention and simplifying the description. Unless otherwise specified, these directional words do not indicate or imply that the device or element referred to must have a specific direction or be constructed and operated in a specific direction. Therefore, they cannot be understood as limiting the scope of protection of the present invention: the directional words "inside and outside" refer to the inside and outside relative to the contours of each component itself.
[0044] Example 1
[0045] A low-temperature infrared radiation coupled biological reaction method, the steps are as follows:
[0046] Reference Figure 1, the original biomass is roughly crushed into biomass material 18, and then the biomass material 18 is naturally piled up, the switch of the infrared irradiation device on the top of the biomass material 18 is turned on, and the biomass material 18 is continuously irradiated by the infrared irradiation device. Under the action of heat generation by microbial fermentation, the temperature of the material 18 is controlled by controlling the power of the infrared irradiation device 4 and the rate of air introduction, so as to provide a stable and suitable environmental temperature for the aerobic fermentation heat generation of microorganisms in the biomass, and the pile is turned twice a day to promote the uniformity of the temperature of the entire material 18 to ensure the efficient progress of the entire microbial reaction; after the reaction is completed (24-72 hours, so that the moisture content of the biomass material 18 after the reaction is reduced to half of the biomass material 18 before the reaction), it is emptied in time, the material 18 is discharged, and new biomass material 18 is filled, and the above operation is repeated to realize continuous operation of the process.
[0047] The biomass material 18 is domestic waste, and the air introduced is air at room temperature. While providing oxygen for the microbial reaction, it can provide rapid heat dissipation when the temperature of the material 18 is too high (higher than the maximum temperature suitable for the survival of microorganisms), ensuring that the temperature of the material 18 is maintained within a suitable ambient temperature range, providing a stable and suitable ambient temperature for the aerobic fermentation heat production of microorganisms in the biomass.
[0048] The temperature of the material 18 is further controlled by controlling the power of the infrared irradiation device 4 and the rate of air introduction to provide a stable and suitable ambient temperature for the microorganisms in the biomass to produce heat through aerobic fermentation. Specifically, it can be:
[0049] When the temperature of the material 18 is lower than the minimum temperature suitable for the survival of microorganisms, the power of the infrared irradiation device 4 is increased, or the rate of air introduction is reduced, or the power of the infrared irradiation device 4 is increased and the rate of air introduction is reduced at the same time, so that the temperature of the material 18 is maintained within a suitable ambient temperature range;
[0050] When the temperature of the material 18 is higher than the maximum temperature suitable for the survival of microorganisms, the air supply rate is increased, or the power of the infrared irradiation device 4 is reduced, or the air supply rate is increased and the power of the infrared irradiation device 4 is reduced at the same time, so that the temperature of the material 18 is maintained within a suitable ambient temperature range.
[0051] Example 2
[0052] A low-temperature infrared radiation coupled biological reaction method, the steps are as follows:
[0053] Reference Figure 1, the raw biomass is roughly crushed into biomass material 18, and then the biomass material 18 is placed in the stirring device, the switch of the infrared irradiation device on the top of the biomass material 18 is turned on, and the infrared irradiation device 4 is used to continuously irradiate the biomass material 18. Under the action of heat generation by microbial fermentation, the temperature of the material 18 is further controlled by controlling the power of the infrared irradiation device 4 and the rate of air introduction, so as to provide a stable and suitable environmental temperature for the aerobic fermentation heat generation of microorganisms in the biomass. Mechanical stirring is performed twice a day to promote the uniformity of the temperature of the entire material 18 to ensure the efficient progress of the entire microbial reaction; after the reaction is completed (24-72 hours, so that the moisture content of the biomass material 18 after the reaction is reduced to half of that of the biomass material 18 before the reaction), it is emptied in time, the material 18 is discharged, and new biomass material 18 is filled, and the above operation is repeated to realize continuous operation of the process.
[0054] The biomass material 18 is kitchen waste, and the air introduced is room temperature air. While providing oxygen for the microbial reaction, it can provide rapid heat dissipation when the temperature of the material 18 is too high (higher than the maximum temperature suitable for the survival of microorganisms), ensuring that the temperature of the material 18 is maintained within a suitable ambient temperature range, providing a stable and suitable ambient temperature for the aerobic fermentation heat production of microorganisms in the biomass.
[0055] The temperature of the material 18 is further controlled by controlling the power of the infrared irradiation device 4 and the rate of air introduction to provide a stable and suitable ambient temperature for the microorganisms in the biomass to produce heat through aerobic fermentation. Specifically, it can be:
[0056] When the temperature of the material 18 is lower than the minimum temperature suitable for the survival of microorganisms, the power of the infrared irradiation device 4 is increased, or the rate of air introduction is reduced, or the power of the infrared irradiation device 4 is increased and the rate of air introduction is reduced at the same time, so that the temperature of the material 18 is maintained within a suitable ambient temperature range;
[0057] When the temperature of the material 18 is higher than the maximum temperature suitable for the survival of microorganisms, the air supply rate is increased, or the power of the infrared irradiation device 4 is reduced, or the air supply rate is increased and the power of the infrared irradiation device 4 is reduced at the same time, so that the temperature of the material 18 is maintained within a suitable ambient temperature range.
[0058] Example 3
[0059] like Figure 2 , 3As shown, a low-temperature infrared radiation coupled biological reaction device comprises: a reactor 8 and an infrared irradiation device 4 and a stirring device arranged inside the reactor 8 from top to bottom, integrating feeding, discharging, material mixing and reaction in one. The upper cover plate 6 of the reactor 8 is located above the lower box 7. The inner wall of the upper cover plate 6 of the reactor 8 is provided with a condensed water collection tank 5 and an infrared irradiation device 4 from top to bottom. The infrared irradiation device 4 is symmetrically arranged on the inner wall of the upper cover plate 6. The condensate collecting tank 5 is symmetrically arranged on the inner wall of the upper cover plate 6, and a feed port 9 and an air outlet 12 are arranged between the top of the upper cover plate 6 and the condensate collecting tank 5, and the feed port 9 and the air outlet 12 are located on both sides of the upper cover plate 6; the bottom of the lower box body 7 of the reactor 8 is provided with a liquid outlet 13, an air inlet 11, and a discharge port 10, and the air inlet 11 is located at the center of the bottom of the lower box body 7, and the liquid outlet 13 and the discharge port 10 are located on both sides of the air inlet 11.
[0060] The biomass material 18 enters the reactor 8 through the feed port 9 at the upper end of the reactor, is heated by the infrared irradiation device 4, is evenly mixed by the stirring device, and a biological reaction occurs. After the reaction is completed, the material 18 is discharged from the discharge port 10 at the lower end of the reactor 8.
[0061] The infrared irradiation device 4 is an infrared irradiation lamp, which is used to provide infrared irradiation to the materials in the reaction kettle 8.
[0062] The stirring device is a twin-screw compost turning shaft, including a forward screw compost turning shaft 1 and a reverse screw compost turning shaft 2. The forward screw compost turning shaft 1 and the reverse screw compost turning shaft 2 are controlled by a driving motor to achieve synchronous operation, and the forward screw compost turning shaft 1 and the reverse screw compost turning shaft 2 rotate in opposite directions.
[0063] The lower box of the reactor 8 has an arc-shaped compost turning plate 3 structure, and a compost turning plate 3 is arranged at the end of one end of the twin-screw compost turning shaft to facilitate the reciprocating movement of the material 18 in the two grooves, so that the reaction is more complete and the material 18 is mixed more evenly.
[0064] The cross section of the upper cover plate 6 of the reactor 8 is a triangular structure, and the condensed water formed on the inner wall surface of the upper cover plate 6 can flow down freely. The condensed water collecting tank 5 above the infrared irradiation device 4 is used to collect the condensed water generated during the process.
[0065] The air inlet 11 at the lower end of the reactor 8 is connected to the low-temperature aeration tank 14, which is used to introduce air into the reactor 8 to provide oxygen for the microbial reaction and avoid anaerobic reaction, so as to facilitate the material 18 to maximize its oxidation function. The introduced air is room temperature air, which can provide oxygen for the microbial reaction and provide rapid heat dissipation when the material temperature is too high (higher than the maximum temperature suitable for the survival of microorganisms), thereby ensuring that the material temperature is maintained within a suitable ambient temperature range and providing a stable and suitable ambient temperature for the aerobic fermentation heat production of microorganisms in the biomass.
[0066] The reactor 8 is provided with a thermocouple for online temperature collection in the reactor 8, and the thermocouple is connected to a temperature controller, an infrared irradiation device 4, and a low-temperature aeration tank 14. The temperature controller is a temperature controller, which controls the temperature of the material 18 by controlling the power of the infrared irradiation device 4 and the rate of air introduction, thereby providing a stable and suitable ambient temperature for aerobic fermentation heat production by microorganisms in the biomass.
[0067] The discharge port at the lower end of the reactor 8 is connected to the solid waste treatment unit 15, and the material discharged from the reactor 8 enters the solid waste treatment unit 15 for solid waste treatment. The gas outlet 12 at the upper end of the reactor 8 is a water vapor channel, and the gas discharged from the reactor 8 enters the waste gas treatment unit 16 for waste gas treatment. The liquid outlet 13 at the lower end of the reactor 8 is connected to the waste liquid treatment unit 17, and the liquid discharged from the reactor 8 enters the waste liquid treatment unit 17 for waste liquid treatment.
[0068] The above-mentioned method for treating biomass waste by using a low-temperature infrared radiation coupled bioreactor comprises the following steps:
[0069] The biomass material 18 enters the reactor 8 through the feed port 9 at the upper end of the reactor 8, the material 18 is irradiated and heated by the infrared irradiation device 4 above the material 18, the material 18 is evenly mixed by the stirring device, and air is introduced into the reactor 8 through the low-temperature aeration tank 14 to provide oxygen for the microbial reaction. After the reaction is completed (24-72 hours), the material 18 is discharged from the discharge port 10 at the lower end of the reactor 8, and new biomass material 18 is filled in, and the above operation is repeated to realize continuous operation of the process.
[0070] The biomass materials include organic matter such as straw, feces, domestic garbage, and kitchen waste, but are not limited to the above.
[0071] Under the action of heat production by microbial fermentation, the temperature of the material 18 is further controlled by controlling the power of the infrared irradiation device 4 and the rate of air introduction, providing a stable and suitable ambient temperature for the aerobic fermentation heat production of microorganisms in the biomass. Mechanical stirring is performed regularly every day to promote the uniformity of the temperature of the entire material 18 to ensure the efficient progress of the entire microbial reaction.
[0072] The temperature of the material 18 is further controlled by controlling the power of the infrared irradiation device 4 and the rate of air introduction to provide a stable and suitable ambient temperature for the microorganisms in the biomass to produce heat through aerobic fermentation. Specifically, it can be:
[0073] When the temperature of the material 18 is lower than the minimum temperature suitable for the survival of microorganisms, the power of the infrared irradiation device 4 is increased, or the rate of air introduction is reduced, or the power of the infrared irradiation device 4 is increased and the rate of air introduction is reduced at the same time, so that the temperature of the material 18 is maintained within a suitable ambient temperature range;
[0074] When the temperature of the material 18 is higher than the maximum temperature suitable for the survival of microorganisms, the air supply rate is increased, or the power of the infrared irradiation device 4 is reduced, or the air supply rate is increased and the power of the infrared irradiation device 4 is reduced at the same time, so that the temperature of the material 18 is maintained within a suitable ambient temperature range.
[0075] The material 18 discharged after the reaction is discharged through the discharge port 10 for solid waste treatment. The gas generated after the reaction is drawn out of the reactor 8 through the induced draft fan for waste gas treatment. The condensed water generated by the reaction is collected by the condensed water collection tank 5, and the liquid generated after the reaction is discharged from the liquid outlet 13 at the lower end of the reactor 8 for waste liquid treatment.
[0076] The present invention couples the traditional biomass microbial aerobic reaction with infrared irradiation, changing the heat transfer from contact to non-contact, and changing the thermal aeration that maintains the material temperature through thermal convection to thermal radiation, which greatly improves the problem that the actual material temperature cannot reach the ideal temperature due to the rapid passage of hot air through the biomass surface, instantly taking away a large amount of water vapor from the biomass surface, and the water evaporation absorbs heat. The entire microbial reaction process is optimized, the microbial reaction activity is greatly improved, the reaction cycle is further shortened, and the reaction efficiency is improved. After the entire microbial reaction process, the moisture content of the biomass material is reduced to half of the original, and the combustion value is improved.
[0077] For any technician familiar with the art, without departing from the scope of the technical solution of the present invention, the technical content disclosed above can be used to make many possible changes and modifications to the technical solution of the present invention, or modified into equivalent embodiments with equivalent changes. Therefore, any simple modification, equivalent change and modification made to the above embodiments according to the technical essence of the present invention without departing from the content of the technical solution of the present invention should still fall within the scope of protection of the technical solution of the present invention.
Claims
1. A low-temperature infrared radiation coupled bioreactor, characterized in that: include: A reactor and an infrared irradiation device and a stirring device arranged inside the reactor from top to bottom, wherein the upper cover plate of the reactor is located above the lower box body, and a condensate collecting tank and an infrared irradiation device are arranged on the inner wall of the upper cover plate of the reactor from top to bottom, and a feed port and an air outlet are arranged between the top of the upper cover plate and the condensate collecting tank, and the feed port and the air outlet are located on both sides of the upper cover plate; a liquid outlet, an air inlet, and a material outlet are arranged at the bottom of the lower box body of the reactor, the air inlet is located at the center of the bottom of the lower box body, and the liquid outlet and the material outlet are located on both sides of the air inlet; The lower box of the reactor has a stack turning plate structure; the cross section of the upper cover plate of the reactor is a triangular structure; The stirring device is a shaft stirring device; The air inlet at the lower end of the reactor is connected to the low-temperature aeration tank; The reactor is provided with a thermocouple for online temperature collection in the reactor, and the thermocouple is connected to a temperature controller, an infrared irradiation device, and a low-temperature aeration tank; The discharge port at the lower end of the reactor is connected to the solid waste treatment unit; the gas outlet at the upper end of the reactor is connected to the waste gas treatment unit; the liquid outlet at the lower end of the reactor is connected to the waste liquid treatment unit; The method for using the low-temperature infrared radiation coupled bioreactor comprises the following steps: The biomass material is naturally piled up or placed in a stirring device, and the biomass material is infrared irradiated by an infrared irradiation device. Under the action of heat generation by microbial fermentation, the temperature of the material is further controlled by controlling the power of the infrared irradiation device and the rate of air introduction, so as to provide a stable and suitable environmental temperature for the aerobic fermentation heat generation of microorganisms in the biomass. By turning the pile or mechanical stirring, the temperature of the whole material is promoted to be uniform to ensure the progress of the whole microbial reaction; after the reaction is completed, the material is discharged and new biomass material is filled in, and the above operation is repeated to realize continuous operation of the process; The biomass material is selected from one or more of straw, feces, and kitchen waste; The air introduced is air at normal temperature; The reaction time is 24-72 hours.
2. The low-temperature infrared radiation coupled bioreactor according to claim 1, characterized in that: The infrared irradiation device is symmetrically arranged on the inner wall of the upper cover plate, and the condensed water collecting tank is symmetrically arranged on the inner wall of the upper cover plate.
Citation Information
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