CN202343551U - Multi-purpose solar organic garbage biochemical processing system - Google Patents

Multi-purpose solar organic garbage biochemical processing system Download PDF

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Publication number
CN202343551U
CN202343551U CN2011203098836U CN201120309883U CN202343551U CN 202343551 U CN202343551 U CN 202343551U CN 2011203098836 U CN2011203098836 U CN 2011203098836U CN 201120309883 U CN201120309883 U CN 201120309883U CN 202343551 U CN202343551 U CN 202343551U
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China
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fermentation dried
assembly
fermentation
connects
water conservancy
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CN2011203098836U
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崔成哲
杨志
崔恩德
崔恩海
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Pu Jiongshan
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Pu Jiongshan
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/133Renewable energy sources, e.g. sunlight
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/20Waste processing or separation

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  • Fertilizers (AREA)

Abstract

Provided is a multi-purpose solar organic garbage biochemical processing system. A fermentation drying assembly with the round cross section is horizontally arranged on a frame and driven by an external speed reducing motor. A solar heat collecting device is arranged above the fermentation drying assembly, n longitudinal hollow material shifting plates are arranged on the inner wall of a fermentation cabin of the fermentation drying assembly, and the hollow material shifting plates are connected through heat conduction tubes. Two tail ends of the heat conduction tubes are respectively connected with internal connection ports of a heat conduction tube external connection assembly, and external connection ports of the heat conduction tube external connection assembly are respectively connected with two ports of an additional heating device. The heat energy required by fermentation drying cabins is supplied by the solar energy and the additional heating device. The multi-purpose solar organic garbage biochemical processing system utilizes a program automatic control to work to strictly control the temperature, the air and the stirring of fermentation materials, and the materials in n fermentation drying cabin can automatically perform quantitative transfer, stirring, fermentation, drying and cabin outlet. The multi-purpose solar organic garbage biochemical processing system saves energy, has high efficiency, and protects the environment, and produced terminal products can be directly used as fertilizers, soil amendment or feed additives.

Description

Multipurpose solar organic waste biochemical treatment system
Technical field
The utility model relates to a kind of multipurpose solar organic waste biochemical treatment system.
Background technology
China's legal provisions; Domestic garbage is wanted categorised collection; Anyone, any unit changing food waste of must not collecting without authorization and circulate without approval particularly; Country advocates and encourages and handles house refuse, changing food waste into resources; Recycling treatment house refuse, changing food waste technology is a lot of in the world at present, and is also very ripe, but have that the operation power consumption is high, cost of investment is high, complex structure, operating technology require high, as to handle back output product not reach national correlation technique standard, produce secondary pollution, need secondary operations etc. that a difficult problem to be solved is arranged.
The utility model content
For solving above-mentioned deficiency, the utility model provides a kind of multipurpose solar organic waste biochemical treatment system that adopts solar energy and the parallel heating of other energy fermentation technique.
The utility model multipurpose solar organic waste biochemical treatment system; Comprise frame (1), fermentation dried assembly (2), solar energy heat collector (3), supplementary heating device (4), heat pipe (5), multi-functional exhaust apparatus (19), circulation heating blower (7), meson circulating pump (8), infrared ray side temperature probe (9); Electric cabinet (10); It is characterized in that; In said frame (1); Cross section of accumbency is the round fermentation dried assembly of rotation (2); Said fermentation dried assembly (2) is provided with the drum shape shell (2-3) by two reducing of N piece arc curve plate (2-1) and two toroidal sealing ends (2-2) combination, and two said toroidal sealing ends (2-2) outer ring connects the circuit orbit circle (2-4) concentric with said shell (2-3) cross section respectively, and said track circle (2-4) is held up by two scroll wheels (17) that are fixed on the said frame (1) respectively; Wherein at least one scroll wheel (17) connects sprocket wheel (17-1), and said sprocket wheel (17-1) is connected with drive sprocket (15-1) on reducing motor (15) axle through chain; Said toroidal sealing end (2-2) outer ring inwall is provided with n root strip center rest (2-5); The centre of said strip center rest (2-5) is provided with adpting flange (2-6); Said adpting flange (2-6) is connected with rotary connector (2-7); Said rotary connector (2-7) inner ring is provided with the bearing holder (housing, cover) (2-7-1) concentric with shell (2-3); The outer ring of said rotary connector (2-7) is provided with mounting flange (2-7-2), is provided with bearing (2-7-3) in the said bearing holder (housing, cover) (2-7-1), and the lateral surface of said rotary connector (2-7) is provided with concentric connection heat pipe and connects the screw hole (2-7-4) that assembly (18) is gone up positioner (11) outward; One interior round mouth of said toroidal sealing end (2-2) is dog-house (14), and round mouth is discharging opening (14-1) in another; It is individual cross-section to shifting board (2-8) to be provided with n in the said fermentation dried assembly (2); Said shifting board (2-8) is separated into n fermentation dried cabin (20) to said fermentation dried assembly (2); The center of circle of said shifting board (2-8) is provided with the material path (2-9) of diameter greater than multifunctional rotary axle (6) diameter; One side of said material path (2-9) is provided with internal diameter greater than transferring material spiral leaf (6-2) external diameter; And the semi-circle tubular charge groove (2-10) concentric with material path (2-9), the length of said charge groove (2-10) is less than the length in fermentation dried cabin, place (20); Said fermentation dried cabin (20) inwall is provided with n vertical hollow switch-plate (2-11), and said hollow switch-plate (2-11) is provided with two fluid import and exports (2-12), and said fluid import and export (2-12) stretches out outside the wall of said fermentation dried cabin (20); The fluid import and export (2-12) of each said hollow switch-plate (2-11) is connected by heat pipe (5), two end ports of said heat pipe (5) respectively with connect mouthful (12-6) in the heat pipe of being located at fermentation dried assembly (2) two ends connects two of assembly (18) outward and be connected; The horizontal multifunctional rotary axle in said fermentation dried assembly (2) center (6); Said multifunctional axial (6) crosses all said fermentation dried cabins (20); One end of wherein said multifunctional axial (6) passes the rotary connector (2-7) and the heat pipe that place fermentation dried assembly (2) one end centres and connects assembly (18) outward; And be connected with reducing motor (16); The other end of said multifunctional axial (6) places on the rotary connector (2-7) in fermentation dried assembly (2) other end centre; Said multifunctional axial (6) is provided with n the tulwar shape reamer (6-1) littler than the space radius in said fermentation dried cabin (20); And be distributed in each said fermentation dried cabin (20); All be provided with an endless belt shape on said multifunctional axial (6) section in each said fermentation dried cabin (20) and transfer material spiral leaf (6-2), said handover material spiral leaf (6-2) is arranged on said multifunctional axial (6) and the inboard staggered section of said charge groove (2-10), and the length of said handover material spiral leaf (6-2) belongs to the length in said fermentation dried cabin (20) less than it; Said solar energy heat collector (3) is arranged at said fermentation dried assembly (2) top; Said solar energy heat collector (3) is provided with vacuum glass cover (3-1); Said vacuum glass cover (3-1) is arranged in the protection framework (3-2); Said protection framework (3-2) is connected with said frame (1), leaves the space between said solar energy heat collector (3) and the said fermentation dried assembly (2), and the two ends of said solar energy heat collector (3) respectively are provided with a closure plate (3-3); Said closure plate (3-3) with the seamless veneer CONTACT WITH FRICTION of both ends of the surface of corresponding said toroidal sealing end (2-2), the contact-making surface material of said closure plate (3-3) is soft nonmetallic composite; Said fermentation dried assembly (2) dog-house (14) upper end is provided with multi-functional exhaust apparatus (19); The discarded air exit that is provided with waste-heat recoverer (19-1), said waste-heat recoverer (19-1) in the said multi-functional exhaust apparatus (19) connects high-frequency impulse dedusting, deodoriser (19-2); The recovery waste heat secondary wind outlet of said waste-heat recoverer (19-1) connects the air inlet of circulation heating blower (7); The air outlet of said circulation heating blower (7) connects ventilation duct (7-1), and said ventilation duct (7-1) connects on the upper end of said fermentation dried assembly (2) discharging opening (14-1); The shell (2-3) that said infrared ray side temperature probe (9) is located at fermentation dried assembly (2) has in the side warming plate (21) of certain space; Said supplementary heating device (4) is provided with air source heat pump (4-1), high temperature heater (HTH) (4-2); The liquid outlet of said air source heat pump (4-1) is connected with the inlet of said high temperature heater (HTH) (4-2); The liquid outlet of said high temperature heater (HTH) (4-2); Connect said heat pipe and connect said outer connect mouthful (13-1) on the assembly (18) outward; The inlet of said air source heat pump (4-1) connects the liquid outlet of said meson circulating pump (8), and the inlet of said meson circulating pump (8) connects said heat pipe and connects another said outer connect mouthful (13-1) on the assembly (18) outward; The used energy of said high temperature heater (HTH) (4-2) is electric energy or for fuel oil or for combustion gas; Said heat pipe connects assembly (18) outward and is provided with cavity tubulose water conservancy diversion axle (13); Said cavity tubulose water conservancy diversion axle (13) is inside and outside wall two-port sealed hollow tubular body; Said cavity tubulose water conservancy diversion axle (13) outer wall is provided with said one outer mouthful (13-1) and n airtight pod apertures (13-2) of connecting; Said one outer mouthful (13-1) and said airtight pod apertures (13-2) all communicate with the cavity of said cavity tubulose water conservancy diversion axle (13); On the section outer wall that is provided with airtight pod apertures (13-2) of said cavity tubulose water conservancy diversion axle (13); Be with cavity tubulose rolling water conservancy diversion cover (12); Said cavity tubulose rolling water conservancy diversion cover (12) is inside and outside wall two-port sealed hollow tubular body; The outer wall two ends of said cavity tubulose rolling water conservancy diversion cover (12) are provided with outer connection blue (12-1), and blue (12-1) both sides of said outer connection connect positioner (11) respectively with one heart, and a said location device (11) connects said rotary connector (2-7) with one heart; Said cavity tubulose rolling water conservancy diversion cover (12) inboard, two ends is provided with spill sealing circular groove (12-2); Said spill sealing circular groove (12-2) inwall is provided with thread, in the said spill sealing circular groove (12-2) sliding ring (12-3) is set, said sliding ring (12-3) arranged outside one annular seal lid (12-4); Said annular seal lid (12-4) outer wall is provided with thread; The thread that is provided with on thread that said annular seal lid (12-4) outer wall is provided with and said spill sealing circular groove (12-2) inwall butt joint that is complementary, the internal diameter of said sealing ring (12-3) is not less than the external diameter of cavity tubulose water conservancy diversion axle (13), and said cavity tubulose rolling water conservancy diversion cover (12) inwall center is provided with annular drainage trough (12-5); Said annular drainage trough (12-5) is facing to the airtight pod apertures (13-2) on cavity tubulose water conservancy diversion axle (13) outer wall; Said annular drainage trough (12-5) and airtight pod apertures (13-2) all place between two sealing rings (12-3), and said cavity tubulose rolling water conservancy diversion cover (12) outer wall is provided with Nei Liankou (12-6), said annular drainage trough (12-5) and said in mouthful (12-6) all communicate with the cavity of said cavity tubulose rolling water conservancy diversion cover (12); Said arc curve plate (2-1) adopts the single-layer metal plate, or adopts the double-layer cavity metallic plate.
The utility model has the advantages that: energy-conservation, efficient, environmental protection, Based Intelligent Control, simple to operate, sturdy and durable, low cost of manufacture, output terminal thing can directly be done the additive of fertilizer, soil conditioner or feed.
Description of drawings
Fig. 1 is the longitudinal section partial sectional view of the utility model multipurpose solar organic waste biochemical treatment system;
Fig. 2 is the utility model multipurpose solar organic waste biochemical treatment system longitudinal section cutaway view;
Fig. 3 is the partial sectional view of fermentation dried assembly (18);
Fig. 4 is the outward appearance front view of fermentation dried assembly (18);
Fig. 5 is arc curve plate (2-1) longitudinal section partial sectional view;
Fig. 6 is rotary connector (2-7) front view;
Fig. 7 is rotary connector (2-7) side view;
Fig. 8 is that heat pipe connects assembly (18) front view outward;
Fig. 9 is that heat pipe connects assembly (18) longitudinal section cutaway view outward;
Figure 10 is that heat pipe connects cavity tubulose rolling water conservancy diversion cover (12) the longitudinal section cutaway view on the assembly (18) outward;
Figure 11 is solar energy heat collector (a 3) stereogram;
Figure 12 is the cross-section partial sectional view of the utility model multipurpose solar organic waste biochemical treatment system.
Specific embodiments
For further setting forth the utility model, make more detailed introduction below in conjunction with embodiment.
Multipurpose solar organic waste biochemical treatment system; Employing serves as main fermentation thermal source with solar radiant heat and natural air heat; With electricity, combustion gas, fuel oil is to replenish the energy, and material stirs voluntarily in a plurality of fermentation dried cabins (20), is shifted, the dry technology of circulating fermentation continuously.
Solar radiant heat and natural air heat are main fermentation thermal source; With electricity, combustion gas, fuel oil is to replenish the energy; Material stirs voluntarily in a plurality of fermentation dried cabins (20), is shifted, the dry technology of circulating fermentation continuously; Be that the main thermal source of showing fermentation dried cabin (20) interior material heating is that solar energy is warm with air source, supplemental heat source is electricity, combustion gas, fuel oil, and the space in the fermentation dried cabin of material is in series by a plurality of independently fermentation dried cabins (20); The material of throwing accomplishes the fermenting procedure of setting in each fermentation dried cabin (20) after; Automatically be transplanted on next fermentation dried cabin (20), continue to do corresponding fermenting procedure, reach complete fermentation and dry purpose by that analogy at last.Temperature required accurately being controlled in 60 ℃ of-62 ℃ of scopes of material fermentation; Material is for a long time under the condition of this temperature and continuous minimizing moisture; Remove acid and alkali resistance that we cultivate voluntarily, salt and weather-proof (temperature, humidity); And outside the specified microorganisms of the diversified material that can ferment, other unhelpful bacteriums can't survive in multistage fermentation dried cabin (20) and breed.Intelligence control system; By the program that is provided with in advance; Strictness controlling a plurality of fermentation dried cabins temperature, humidity, contain the oxygen air; Material feeding amount between the rotation stirring speed in the accurate fermentation dried cabin of control of while (20), mixing time, fermentation dried cabin (20), material fully contact the aerobic air in each fermentation dried cabin (20), and temperature required, the humidity of the quick breeding of acquisition fermentative microflora; The material that make continuous timing, quantitatively drops into, the constantly automatic overall process of accomplishing staged fermentation, drying, deliver from vault in fermentation dried cabin.As being not suitable for gathering the bad weather of solar energy, system will start supplementary heating device (4) automatically, force to carry fermentation institute energy requirement to fermentation dried cabin (20).
Multipurpose solar organic waste biochemical treatment system is made up of following five parts altogether:
1. solar thermal collection system.Shown in figure 11, solar thermal collection system is made up of vacuum glass cover (3-1), protection framework (3-2).Vacuum glass cover (3-1) is installed in the protection framework (3-2), forms relatively independent solar energy heat collector (3); As shown in Figure 1, leave the space between solar energy heat collector (3) and the fermentation dried assembly (2), in order to avoid fermentation dried assembly (2) when being rotated operation and vacuum glass cover (3-1) bump.In order to prevent that the heat of collection between fermentation dried assembly (2) and vacuum glass cover (3-1) runs off; The two ends of solar energy heat collector (3) respectively are provided with a closure plate (3-3); Closure plate (3-3) with the seamless CONTACT WITH FRICTION of toroidal sealing end (2-2) face at shell (2-3) two ends of corresponding fermentation dried assembly (2); The contact-making surface material of closure plate (3-3) is nonmetal soft composite material. therefore, even fermentation dried assembly (2) is rotated operation, heat can not run off yet.Fully gather solar radiation heat energy in order to make solar energy heat collector (3); And the energy of being gathered is given the material in the fermentation dried cabin (20) by shell (2-3) absorption and the conduction of fermentation dried assembly (2); Solar energy heat collector (3) places fermentation dried assembly (2) top, and protection framework (3-2) is connected on the frame (1).For solar energy heat collector easy to maintenance (3) can be divided into two or more.
2. fermentation dried system.Shown in figure (2); Fermentation dried system connects assembly (18) outward by shell (2-3), shifting board (2-8), multifunctional axial (6) rotary connector (2-7), charge groove (2-10), hollow switch-plate (2-11), heat pipe (5), heat pipe and forms fermentation dried assembly (2).Shell (2-3) is combined as scheming arc curve plate (2-1) shown in (5) and two toroidal sealing ends (2-2) by the n piece; Shape is like the drum like two reducing; Said arc curve plate (2-1) adopts the single-layer metal plate; Also can adopt the double-layer cavity metallic plate, the ring outer wall setting circuit orbit circle (2-4) concentric outside toroidal sealing end (2-2) with shell (2-3) cross section.Shown in figure (12); Each track circle (2-4) is held up by two scroll wheels (17) that are fixed on the frame (1) respectively; Wherein at least one scroll wheel (17) connects sprocket wheel (17-1); Sprocket wheel (17-1) is connected with drive sprocket (15-1) on reducing motor (15) axle through chain, drives fermentation dried assembly (2) and rotates.Toroidal sealing end (2-2) the outer ring inwall of fermentation dried assembly (2) is provided with strip center rest (2-5) shown in figure (3); The centre of strip center rest (2-5) is provided with adpting flange (2-6), adpting flange (2-6) be located at rotary connector (2-7) on concentric connection of mounting flange (2-7-2).Shown in figure (6); Rotary connector (2-7) is provided with bearing holder (housing, cover) (2-7-1); The outer ring of bearing holder (housing, cover) (2-7-1) is provided with mounting flange (2-7-2); Bearing (2-7-3) is set in the bearing holder (housing, cover) (2-7-1), and another lateral surface of rotary connector (2-7) is provided with n and connects the fixed screw holes (2-7-4) that heat pipe connects assembly (18) outward with one heart.Heat pipe connects assembly (18) two ends outward outer connection orchid (12-1) is set respectively shown in figure (9); Two outer connections blue (12-1) are located concentric connection of flange (11-1) with one of positioner (11) respectively, and heat pipe connects assembly (18) outward and positioner (11), rotary connector (2-7) are fixed with screw.The two ends of fermentation dried assembly (2) are provided with toroidal sealing end (2-2) respectively shown in figure (2); The interior open ports of the toroidal sealing end (2-2) that wherein is connected with the air outlet of circulation heating blower (7) is discharging opening (14-1); The other end is dog-house (14); Shown in figure (2); Shifting board (2-8) is separated into n fermentation dried cabin (20) to the interior cabin of fermentation dried assembly (2); The material path (2-9) of diameter greater than multifunctional axial (6) diameter is set on the center of circle of each shifting board (2-8), and the same side of each material path (2-9) is provided with internal diameter greater than the semi-circle tubular charge groove (2-10) of transferring material spiral leaf (2) external diameter and material path (2-9) internal diameter, and the length of charge groove (2-10) belongs to the width of fermentation dried cabin (20) less than charge groove (2-10); N vertical hollow switch-plate (2-11) is set in each fermentation dried cabin (20); Evenly be periphery on the bulkhead of fermentation dried cabin (20), hollow switch-plate (2-11) is provided with fluid import and export (2-12), and fluid import and export (2-12) port stretches out outside the arc curve plate (2-1) in fermentation dried cabin (20).Shown in figure (4); Heat pipe (5) is at arc curve plate (2-1) outer wall; Fluid import and export (2-12) the port connection parallel with one another of hollow switch-plate (2-11), two end ports of heat pipe (5) are connected the heat that external complement heater (4) provides with the Nei Liankou (12-6) that the heat pipe of being located at fermentation dried assembly (2) two ends connects assembly (18) outward respectively; Get into each hollow switch-plate (2-11) through the heat conduction meson heat pipe (5) of flowing through; Be discharged in the fermentation dried cabin (20), make when not having the sun or sunlight deficiency, guarantee to supply with each fermentation dried cabin (20) the fermentation dried institute of interior material energy requirement; Shown in figure (3); Multifunctional axial (6) crosses said fermentation dried cabin (20), and wherein an end of multifunctional axial (6) passes the rotary connector (2-7) that places fermentation dried assembly (2) one end centres and the heat pipe that links to each other with rotary connector (2-7) connects assembly (18) outward, and is connected with reducing motor (16); The other end of multifunctional axial (6) places on the rotary connector (2-7) in fermentation dried assembly (2) other end centre; Make said multifunctional axial (6) and said fermentation dried assembly (2) shell (2-3) form with one heart and can carry out the linkage structure of relative rotary motion, on multifunctional axial (6) section in each fermentation dried cabin (20), be arranged side by side n tulwar shape reamer (6-1) and an endless belt shape littler and transfer material spiral leaf (6-2) than space, the interior cabin of fermentation dried assembly (2) radius; Transferring material spiral leaf (6-2) is arranged on multifunctional axial (6) and the inboard staggered section of charge groove (2-10); The length of transferring material spiral leaf (6-2) belongs to the length of fermentation dried cabin (20) less than it, when the shell (2-3) of fermentation dried assembly (2) under the drive of the scroll wheel (17) that links to each other with reducing motor (15), relative frame (1) is when doing rolling movement; The interior material in fermentation dried cabin (20) is at the moving upward displacement down of the holder of hollow switch-plate (2-11); Material is shed to voluntarily under the drive of reducing motor (16) when the material holder moves on to the circumference top, and on tulwar shape reamer (6-1) on setting that opposite shell (2-3) rotates and the multifunctional axial (6) and the handover material spiral leaf (6-2), the tulwar shape reamer (6-1) of rotation and handover material spiral leaf (6-2) are broken the material group that falls above that; Material in the cabin is evenly stirred at this moment; Be not shifted into other fermentation dried cabin, when needs were transplanted on material in adjacent fermentation dried cabin, multifunctional axial (6) drives to be transferred material spiral leaf (6-2) and transfers the material rotation program; Be transplanted on adjacent fermentation dried cabin (2) to the material dosing that drops in the charge groove (2-10); After accomplishing handover material program, multifunctional axial (6) is returned to only to do and stirs material in the cabin, does not do the program of material to other fermentation dried cabin (2) of transferring; By that analogy, material is successively automatically accomplished in each fermentation dried cabin (2) and is stirred, broken, fermentation, quantitatively is transplanted on the program of another fermentation dried cabin (2), deliver from vault.
3) supplemental heat source feed system.As shown in Figure 1; For the interior material in fermentation dried cabin (20) under the weather conditions that do not have sunlight or sunlight deficiency, also can normally be fermented; Be connected in series by high temperature heater (HTH) (4-2), air source heat pump (4-1) and form energy resource supply supplementary heating device (4), supplementary heating device (4) can be connected with solar thermal collection system independently; The meson circulating pump (8) that links together with high temperature heater (HTH) (4-2) and air source heat pump (4-1); Conduct meson to the elevated temperature heat that supplementary heating device (4) provides; Be transported to hollow switch-plate (2-11) through heat pipe (5) circulation; In fermentation dried cabin (20), get back to supplementary heating device (4) after the acting heat release cooling and reheat, move in circles.
Concrete grammar is; The inlet of meson circulating pump (8) is connected to a heat pipe with heat pipe (5) and connects the Wai Liankou (13-1) on the assembly (18) outward; Meson circulating pump (8), air source heat pump (4-1), high temperature heater (HTH) (4-2) are chained together; The liquid outlet of high temperature heater (HTH) (4-2) is connected to heat pipe with heat pipe (5) and connects another outer connect mouthful (13-1) on the assembly (18) outward, and the used energy of high temperature heater (HTH) (4-2) is electric energy or for fuel oil or be combustion gas.When night operation or meet when being not suitable for gathering the bad weather of solar energy, system will start supplementary heating device (4) automatically, force to carry fermentation institute energy requirement to fermentation dried cabin (20) through cycling hot conduction meson.The optimum condition temperature range of air source heat pump (4-1) for be no more than 55 ℃ (; Air source heat pump (4-1) is heated to the 55 ℃ of scopes that are no more than to liquid heat conduction meson (moisture, anti-icing fluid, heat conduction wet goods) in maximum energy-saving operating mode scope; By high temperature heater (HTH) (4-2) temperature from air source heat pump (4-1) output is heated to 65 ℃ of-80 ℃ of scopes at the conduction of the liquid heat below 55 ℃ meson again; Meson circulating pump (8) constantly is transported to the hollow switch-plate (2-11) in the fermentation dried cabin (20) to the heat conduction meson circulation that is heated to 65 ℃ of-80 ℃ of scopes; And acting heat release in fermentation dried cabin (20); Guarantee 60 ℃ of required constant temperature of material fermentation; Summer (outdoor minimum temperature is higher than 15 ℃), the evenly heat effect of air source heat pump (4-1) can reach 1: 4 than (cop), and evenly heat was imitated and can be reached 1: 2 than (cop) winter (outdoor mean temperature is higher than 0 ℃), so energy-saving effect is very outstanding.
4) the heat conduction meson circulatory system.During the native system operation; The heat pipe (5) that is connected on the supplementary heating device (4) is in static state; The heat pipe (5) that is connected on the fermentation dried cabin (20) is in dynamically; Be in the heat conduction meson in the static heat pipe (5) in order to let, constantly safety flows into dynamic heat pipe (5), and circulates; We are at static heat pipe (5) with dynamically between the heat pipe (5); Be provided with the heat pipe of being made up of cavity tubulose water conservancy diversion axle (13), cavity tubulose rolling water conservancy diversion cover (12) and positioner (11) and connect assembly (18) outward, cavity tubulose water conservancy diversion axle (13) is the cavity tubular body of inside and outside wall closed at both ends, is provided with one on cavity tubulose water conservancy diversion axle (13) outer wall and connects mouthful (13-1) outward; Again with connect mouthful (13-1) outward and greater than the circumference place of 2cm one or n airtight pod apertures (13-2) be set at interval; Mouthful (13-1) and airtight pod apertures (13-2) all are communicated with the cavity of cavity tubulose water conservancy diversion axle (13) outward, and Wai Liankou (13-1) is connected in the liquid outlet of supplementary heating device (4) through heat pipe (5), and cavity tubulose water conservancy diversion axle (13) is static state when working; Shown in figure 10, cavity tubulose rolling water conservancy diversion cover (12) is the cavity tubular body of inside and outside wall closed at both ends, and cavity tubulose rolling water conservancy diversion cover (12) outer wall is provided with Nei Liankou (12-6); The inwall center is provided with annular drainage trough (12-5); Cavity tubulose rolling water conservancy diversion cover (12) two ends are respectively equipped with spill sealing circular groove (12-2), and spill sealing circular groove (12-2) inwall is provided with the internal thread button, and is as shown in Figure 9; In the spill sealing circular groove (12-2) sliding ring (12-3) is set; The outer annular seal lid (12-4) that is provided with of sliding ring (12-3), annular seal lid (12-4) outer wall is provided with the outside nut button, the butt joint that is complementary of outside nut button and said internal thread button; Regulate the degree of tightness of ring-type seal cover (12-4), control sliding ring (12-3) is to the seal degree of cavity tubulose water conservancy diversion axle (13) with cavity tubulose rolling water conservancy diversion cover (12) junction surface.The outer wall two ends of cavity tubulose rolling water conservancy diversion cover (12) are respectively equipped with outer connection blue (12-1); Two outer connections blue (12-1) respectively with location concentric a connection of flange (11-1) that places positioner (11) two ends, another locating flange (11-1) on the positioner (11) is connected with rotary connector (2-7) with one heart; Positioner (11) inner ring is provided with the bearing (11-2) of internal diameter and cavity tubulose water conservancy diversion axle (13) external diameter coupling.As shown in Figure 8; Two ends are provided with the cavity tubulose rolling water conservancy diversion cover (12) of positioner (11); Be enclosed within on the outer wall of the cavity tubulose water conservancy diversion axle (13) that is provided with airtight pod apertures (13-2); As shown in Figure 9, it is concentric with cavity tubulose rolling water conservancy diversion cover (12) that bearing (11-2) on two positioners (11) guarantees to be through the cavity tubulose water conservancy diversion axle (13) of its inner ring.Annular drainage trough (12-5) is facing to airtight pod apertures (13-2); Annular drainage trough (12-5) and airtight pod apertures (13-2) all are clipped between two sealing rings (12-3); Form the cavity of the static cavity tubulose water conservancy diversion axle of connection (13) and the loose joint confined space of dynamic cavity tubulose rolling water conservancy diversion cover (12) cavity; Nei Liankou (12-6) on cavity tubulose rolling water conservancy diversion cover (12) outer wall; An end port that connects the heat pipe (5) that places fermentation dried assembly (2); When fermentation dried cabin (20) when rotating; The positioner (11) and the cavity tubulose rolling water conservancy diversion cover (12) that connect together with rotary connector (2-7) rotate synchronously, and two sealing rings (12-3) of cavity tubulose rolling water conservancy diversion cover (12) are sealing the slit between cavity tubulose rolling water conservancy diversion cover (12) and the cavity tubulose water conservancy diversion axle (13), and the heat conduction meson after realizing being heated is from supplementary heating device (4) liquid outlet; Get into the cavity body of cavity tubulose water conservancy diversion axle (13) through the Wai Liankou (13-1) of static cavity tubulose water conservancy diversion axle (13); Flow out from airtight pod apertures (13-2), the dynamic airtight spatial transition that is formed by two sealing rings (12-3) and annular drainage trough (12-5) on the cavity tubulose rolling water conservancy diversion cover (12) of flowing through is in dynamic cavity tubulose rolling water conservancy diversion cover (12) cavity body that rotates of axle center through annular drainage trough (12-5) entering with cavity tubulose water conservancy diversion axle (13) more again; Flow out from interior connect mouthful (12-6) again; Get into hollow switch-plate (2-11) the acting heat release in the fermentation dried cabin through heat pipe (5), the cooled heat of heat release is conducted meson, outside the heat pipe that is arranged at fermentation dried assembly (2) other end, connects assembly (18) Nei Liankou (12-6) and flows to and connect assembly (18) outside the heat pipe; From outside connect mouthful (13-1) and flow back into supplementary heating device (4) and heat, move in circles by that analogy.
5) multi-functionally give, exhaust apparatus.As shown in Figure 2, fermentation dried assembly (2) dog-house (14) upper end is provided with multi-functional exhaust apparatus (19), and multi-functional exhaust apparatus (12) is made up of waste-heat recoverer (19-1) and high-frequency impulse dedusting, deodoriser (19-2).The air inlet of waste-heat recoverer (19-1) is connected to the upper end of dog-house (14) with the exhaust pipe fitting; The exhaust pipe fitting attracts to get into waste-heat recoverer (19-1) from the vapours that dog-house (14) is discharged; Its heat is absorbed by the circulated air through waste-heat recoverer (19-1) secondary air channel; The exhaust end of waste-heat recoverer (19-1) connects high-frequency impulse dedusting, deodoriser (19-2), and high-frequency impulse dedusting, deodoriser are with the dust in high pressure, the pulse current absorption exhaust; Plasma discharge is being contained in the peculiar smell molecular breakdown in the exhaust, and the gas that finally effluxes is gas up to standard dustless, free from extraneous odour.The recovery waste heat secondary wind outlet of waste-heat recoverer (19-1) connects the air inlet of circulation heating blower (7); The air outlet of circulation heating blower (7) connects fermentation dried assembly (2) discharging opening (14-1) upper end through ventilation duct (7-1); Through controlling wind speed, air quantity, the temperature that circulation heating blower (7) is blown into discharging opening (14-1) upper end air, regulate humidity and oxygen content in the fermentation dried cabin.
6) electric-control system.By liquid crystal touch screen, PLC, relay, infrared temperature sensor, frequency converter, form electric cabinet (10).Actual conditions according to the environment for use and the material handling of wanting; Working procedure is set; Working procedure is apparent in touch-screen, can use manual, automatic, that the Long-distance Control mode is controlled fermentation dried assembly (2) and multifunctional axial (6) rotation direction, rotating speed, stirs material as required, transfers inventory; Control circulation heating blower (7) and supplementary heating device (4) are regulated oxygenating amount and temperature in the fermentation dried assembly (2), and the material that make continuous timing, quantitatively drops into is accomplished the overall process of fermentation dried and deliver from vault automatically.
The operation principle of multipurpose solar organic waste biochemical treatment system is: the microorganism species for preparing moisture and the biological medium compound that can fill with fermentation dried cabin (20) working position; Put into first fermentation dried cabin (20) in right amount in batches; The interior temperature in fermentation dried cabin (20) is set at 60 degrees centigrade; Start and connect fermentation dried assembly (2) reducing motor (15) and the reducing motor that is connected multifunctional axial (6) (16); Make the shell (2-3) and multifunctional axial (6) rotation relatively of fermentation dried assembly (2); Multifunctional axial (6) is set to carry out and is transferred the material program, and when fermentation dried cabin (20) rotated, hollow switch-plate (2-11) upward displacement to collection in the material holder of fermentation dried cabin (20) bottom; When hollow switch-plate (2-11) forwards the circumference top to; Material above that is shed to being arranged on the tulwar shape reamer (6-1) and handover material spiral leaf (6-2) and charge groove (2-10) on the multifunctional axial (6) of rotating voluntarily, and the tulwar shape reamer (6-1) of rotation is broken and evenly stirring the material group that falls above that, transfers material spiral leaf (2) and is transplanted on adjacent fermentation dried cabin (20) to the material that drops in the charge groove (2-10); After treating that a mixed material for preparing is all put into fermentation dried cabin (20); Adjustment multifunctional axial (6) is only done stirring 10 minutes repeatedly, static 10 minutes working procedure, moves 120 hours always, and the compound in fermentation dried cabin this moment (20) obtains fermentation fully.The working procedure of at this time fermentation dried assembly (2) is adjusted into fermentation dried cabin (20) and multifunctional axial (6) rotates stirring after 10 minutes, static 10 minutes simultaneously; Carry out the action of 1 minute handover material with the fermentation dried thing of discharging; Every day is according to the day output of equipment afterwards; Throw into first fermentation dried cabin (20) to material to be fermented regularly, quantitatively, in batches; Intelligent electric-controlled system is control fermentation dried assembly (2) and energy supplementary device (4) automatically, continuously to the material in the fermentation dried cabin of new entering (20) mix, heat, stir, ferment, whole programs of drying, emission product.In this process; The institute's calorific requirement of fermenting daytime is mainly supplied with by solar energy heat collector (3); When not having sunlight or sunlight not enough, fermentation institute calorific requirement is the mode through heat pipe (5) circulating heat conduction meson mainly, the heat that the supplementary heating device of being made up of air source heat pump (4-1) and high temperature heater (HTH) (4-2) (4) or external independent solar acquisition system are provided; Be transported in the fermentation dried cabin (20), make fermentation materials obtain the required energy of fermentation.The a large amount of steam that produce in the material sweat; Blast pipe through being arranged on dog-house (14) top is drawn into waste-heat recoverer (19-1); Lowered the temperature, fallen through heat exchange that wet waste gas gets into the high-frequency impulse dedusting again, deodoriser (19-2) purifies and deodorizing, be discharged in the atmosphere after reaching environmental emission standard.Outdoor air through waste-heat recoverer (19-1) heat exchange heats up after circulation heating blower (7) heating, is blown into fermentation dried cabin (20) from discharging opening (14-1) again, regulates keeping and humidity in the fermentation dried cabin (20).
Fig. 5 is arc curve plate (2-1) longitudinal section partial sectional view; The fermentation dried cabin (20) of series connection display side by side in the shell (2-3) of visual fermentation dried assembly (2) among the figure; Arc curve plate (2-1) adopts the single-layer metal plate structure, also can adopt double-level-metal plate cavity structure.
Multipurpose solar organic waste biochemical treatment system; Adopting solar energy and air source heat is the technology of thermal source of mainly fermenting, the standard that energy-saving effect is remarkable, automaticity is high, work continuously, non-secondary pollution, output object reach organic chemical fertilizer or the animal feed additive that can directly pack circulation.

Claims (4)

1. multipurpose solar organic waste biochemical treatment system; Comprise frame (1), fermentation dried assembly (2), solar energy heat collector (3), supplementary heating device (4), heat pipe (5), multi-functional exhaust apparatus (19), circulation heating blower (7), meson circulating pump (8), infrared ray side temperature probe (9); Electric cabinet (10); It is characterized in that; In said frame (1); Cross section of accumbency is the round fermentation dried assembly of rotation (2); Said fermentation dried assembly (2) is provided with the drum shape shell (2-3) by two reducing of N piece arc curve plate (2-1) and two toroidal sealing ends (2-2) combination, and two said toroidal sealing ends (2-2) outer ring connects the circuit orbit circle (2-4) concentric with said shell (2-3) cross section respectively, and said track circle (2-4) is held up by two scroll wheels (17) that are fixed on the said frame (1) respectively; Wherein at least one scroll wheel (17) connects sprocket wheel (17-1), and said sprocket wheel (17-1) is connected with drive sprocket (15-1) on reducing motor (15) axle through chain; Said toroidal sealing end (2-2) outer ring inwall is provided with n root strip center rest (2-5); The centre of said strip center rest (2-5) is provided with adpting flange (2-6); Said adpting flange (2-6) is connected with rotary connector (2-7); Said rotary connector (2-7) inner ring is provided with the bearing holder (housing, cover) (2-7-1) concentric with shell (2-3); The outer ring of said rotary connector (2-7) is provided with mounting flange (2-7-2), is provided with bearing (2-7-3) in the said bearing holder (housing, cover) (2-7-1), and the lateral surface of said rotary connector (2-7) is provided with concentric connection heat pipe and connects the screw hole (2-7-4) that assembly (18) is gone up positioner (11) outward; One interior round mouth of said toroidal sealing end (2-2) is dog-house (14), and round mouth is discharging opening (14-1) in another; It is individual cross-section to shifting board (2-8) to be provided with n in the said fermentation dried assembly (2); Said shifting board (2-8) is separated into n fermentation dried cabin (20) to said fermentation dried assembly (2); The center of circle of said shifting board (2-8) is provided with the material path (2-9) of diameter greater than multifunctional rotary axle (6) diameter; One side of said material path (2-9) is provided with internal diameter greater than transferring material spiral leaf (6-2) external diameter; And the semi-circle tubular charge groove (2-10) concentric with material path (2-9), the length of said charge groove (2-10) is less than the length in fermentation dried cabin, place (20); Said fermentation dried cabin (20) inwall is provided with n vertical hollow switch-plate (2-11), and said hollow switch-plate (2-11) is provided with two fluid import and exports (2-12), and said fluid import and export (2-12) stretches out outside the wall of said fermentation dried cabin (20); The fluid import and export (2-12) of each said hollow switch-plate (2-11) is connected by heat pipe (5), two end ports of said heat pipe (5) respectively with connect mouthful (12-6) in the heat pipe of being located at fermentation dried assembly (2) two ends connects two of assembly (18) outward and be connected; The horizontal multifunctional rotary axle in said fermentation dried assembly (2) center (6); Said multifunctional axial (6) crosses all said fermentation dried cabins (20); One end of wherein said multifunctional axial (6) passes the rotary connector (2-7) and the heat pipe that place fermentation dried assembly (2) one end centres and connects assembly (18) outward; And be connected with reducing motor (16); The other end of said multifunctional axial (6) places on the rotary connector (2-7) in fermentation dried assembly (2) other end centre; Said multifunctional axial (6) is provided with n the tulwar shape reamer (6-1) littler than the space radius in said fermentation dried cabin (20); And be distributed in each said fermentation dried cabin (20); All be provided with an endless belt shape on said multifunctional axial (6) section in each said fermentation dried cabin (20) and transfer material spiral leaf (6-2), said handover material spiral leaf (6-2) is arranged on said multifunctional axial (6) and the inboard staggered section of said charge groove (2-10), and the length of said handover material spiral leaf (6-2) belongs to the length in said fermentation dried cabin (20) less than it; Said solar energy heat collector (3) is arranged at said fermentation dried assembly (2) top; Said solar energy heat collector (3) is provided with vacuum glass cover (3-1); Said vacuum glass cover (3-1) is arranged in the protection framework (3-2); Said protection framework (3-2) is connected with said frame (1), leaves the space between said solar energy heat collector (3) and the said fermentation dried assembly (2), and the two ends of said solar energy heat collector (3) respectively are provided with a closure plate (3-3); Said closure plate (3-3) with the seamless veneer CONTACT WITH FRICTION of both ends of the surface of corresponding said toroidal sealing end (2-2), the contact-making surface material of said closure plate (3-3) is soft nonmetallic composite; Said fermentation dried assembly (2) dog-house (14) upper end is provided with multi-functional exhaust apparatus (19); The discarded air exit that is provided with waste-heat recoverer (19-1), said waste-heat recoverer (19-1) in the said multi-functional exhaust apparatus (19) connects high-frequency impulse dedusting, deodoriser (19-2); The recovery waste heat secondary wind outlet of said waste-heat recoverer (19-1) connects the air inlet of circulation heating blower (7); The air outlet of said circulation heating blower (7) connects ventilation duct (7-1), and said ventilation duct (7-1) connects on the upper end of said fermentation dried assembly (2) discharging opening (14-1); The shell (2-3) that said infrared ray side temperature probe (9) is located at fermentation dried assembly (2) has in the side warming plate (21) of certain space.
2. according to the multipurpose solar organic waste biochemical treatment system of claim 1; It is characterized in that said supplementary heating device (4) is provided with air source heat pump (4-1), high temperature heater (HTH) (4-2); The liquid outlet of said air source heat pump (4-1) is connected with the inlet of said high temperature heater (HTH) (4-2); The liquid outlet of said high temperature heater (HTH) (4-2) connects said heat pipe and connects said outer connect mouthful (13-1) on the assembly (18) outward, and the inlet of said air source heat pump (4-1) connects the liquid outlet of said meson circulating pump (8); The inlet of said meson circulating pump (8) connects said heat pipe and connects another said outer connect mouthful (13-1) on the assembly (18) outward; The used energy of said high temperature heater (HTH) (42) is electric energy or for fuel oil or for combustion gas.
3. according to the multipurpose solar organic waste biochemical treatment system of claim 1; It is characterized in that said heat pipe connects assembly (18) outward and is provided with cavity tubulose water conservancy diversion axle (13); Said cavity tubulose water conservancy diversion axle (13) is inside and outside wall two-port sealed hollow tubular body; Said cavity tubulose water conservancy diversion axle (13) outer wall is provided with said one outer mouthful (13-1) and n airtight pod apertures (13-2) of connecting; Said one outer mouthful (13-1) and said airtight pod apertures (13-2) all communicate with the cavity of said cavity tubulose water conservancy diversion axle (13); On the section outer wall that is provided with airtight pod apertures (13-2) of said cavity tubulose water conservancy diversion axle (13); Be with cavity tubulose rolling water conservancy diversion cover (12), said cavity tubulose rolling water conservancy diversion cover (12) is inside and outside wall two-port sealed hollow tubular body, and the outer wall two ends of said cavity tubulose rolling water conservancy diversion cover (12) are provided with outer connection blue (12-1); Blue (12-1) both sides of said outer connection connect positioner (11) respectively with one heart; A said location device (11) connects said rotary connector (2-7) with one heart, and said cavity tubulose rolling water conservancy diversion cover (12) inboard, two ends is provided with spill sealing circular groove (12-2), and said spill sealing circular groove (12-2) inwall is provided with thread; In the said spill sealing circular groove (12-2) sliding ring (12-3) is set; Said sliding ring (12-3) arranged outside one annular seal lid (12-4), said annular seal lid (12-4) outer wall is provided with thread, the thread that is provided with on thread that said annular seal lid (12-4) outer wall is provided with and said spill sealing circular groove (12-2) inwall butt joint that is complementary; The internal diameter of said sealing ring (12-3) is not less than the external diameter of cavity tubulose water conservancy diversion axle (13); Said cavity tubulose rolling water conservancy diversion cover (12) inwall center is provided with annular drainage trough (12-5), and said annular drainage trough (12-5) is facing to the airtight pod apertures (13-2) on cavity tubulose water conservancy diversion axle (13) outer wall, and said annular drainage trough (12-5) and airtight pod apertures (13-2) all place between two sealing rings (12-3); Said cavity tubulose rolling water conservancy diversion cover (12) outer wall is provided with Nei Liankou (12-6), said annular drainage trough (12-5) and said in mouthful (12-6) all communicate with the cavity of said cavity tubulose rolling water conservancy diversion cover (12).
4. according to the multipurpose solar organic waste biochemical treatment system of claim 1, it is characterized in that said arc curve plate (2-1) adopts the single-layer metal plate, or adopt the double-layer cavity metallic plate.
CN2011203098836U 2011-08-24 2011-08-24 Multi-purpose solar organic garbage biochemical processing system Expired - Lifetime CN202343551U (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104154238A (en) * 2014-07-31 2014-11-19 三零一(深圳)环保科技有限公司 Sealing device capable of partitioning outer cavity of rotary drum and rotary heating device with sealing device
CN105290086A (en) * 2015-11-13 2016-02-03 浙江国千环境科技股份有限公司 Device for processing kitchen garbage through microorganism fermentation method
CN107755404A (en) * 2017-03-17 2018-03-06 青岛陶知电子科技有限公司 A kind of intelligent kitchen garbage processing system
CN109746248A (en) * 2019-01-21 2019-05-14 广州好美环保技术有限公司 A kind of organic waste innocent treatment equipment
CN113732018A (en) * 2021-09-03 2021-12-03 北京嘉博文生物科技有限公司 Continuous organic garbage biological treatment machine
CN114350500A (en) * 2022-03-18 2022-04-15 领先生物农业股份有限公司 Membrane-covered aerobic fermentation circulating device and circulating method

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104154238A (en) * 2014-07-31 2014-11-19 三零一(深圳)环保科技有限公司 Sealing device capable of partitioning outer cavity of rotary drum and rotary heating device with sealing device
CN104154238B (en) * 2014-07-31 2016-03-16 三零一(深圳)环保科技有限公司 A kind of seal arrangement and rotary type heating equipment thereof of isolating revolving drum exocoel
CN105290086A (en) * 2015-11-13 2016-02-03 浙江国千环境科技股份有限公司 Device for processing kitchen garbage through microorganism fermentation method
CN105290086B (en) * 2015-11-13 2017-10-10 浙江国千环境科技股份有限公司 A kind of microbial fermentation processes handle the device of kitchen garbage
CN107755404A (en) * 2017-03-17 2018-03-06 青岛陶知电子科技有限公司 A kind of intelligent kitchen garbage processing system
CN109746248A (en) * 2019-01-21 2019-05-14 广州好美环保技术有限公司 A kind of organic waste innocent treatment equipment
CN113732018A (en) * 2021-09-03 2021-12-03 北京嘉博文生物科技有限公司 Continuous organic garbage biological treatment machine
CN114350500A (en) * 2022-03-18 2022-04-15 领先生物农业股份有限公司 Membrane-covered aerobic fermentation circulating device and circulating method
CN114350500B (en) * 2022-03-18 2022-06-03 领先生物农业股份有限公司 Membrane-covered aerobic fermentation circulating device and circulating method

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