CN104163667A - Improved rapid thermal enzyme treating device for recycling organic waste - Google Patents
Improved rapid thermal enzyme treating device for recycling organic waste Download PDFInfo
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- CN104163667A CN104163667A CN201410239925.1A CN201410239925A CN104163667A CN 104163667 A CN104163667 A CN 104163667A CN 201410239925 A CN201410239925 A CN 201410239925A CN 104163667 A CN104163667 A CN 104163667A
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
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Abstract
The invention discloses an improved rapid thermal enzyme treating device for recycling organic wastes. The device is composed of a rack, a U-shaped reaction kettle, a motor, a gear transmission device, a speed reducer, a hammerhead stirring blade, a reaction kettle outer wall filling material layer, a U-shaped reaction kettle outer steel plate, an electric heating plate, a temperature controller, two pairs of electric blowers, an electric control cabinet, one or more group of weir type top covers, a horn-shaped feeding opening, exhaust ports with filter screens, an acrylic glass observation window, an automatic discharge air valve switch and an aerial fog separator. The top of the reaction kettle is changed to a weir type structure from an original flat structure; and one end of the fixed top cover is provided with one horn-shaped feeding opening with a plug and three exhaust ports with the filter screens. The improved rapid thermal enzyme treating device for recycling the organic wastes has the effects of collecting moisture and removing odors while meeting thermal enzyme fermentation of the wastes and finishing recycling utilization in 18-24 hours. The fermentation process can effectively reduce energy consumption by 10%-30%.
Description
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Technical field
The invention belongs to the comprehensive utilization of environment environmental protection and renewable resource and relate to technical field, relate in particular to reclaiming organic waste Rapid Thermal enzyme treatment facility.
Background technology
As prior art, Chinese patent (CN201320323568.8) discloses a kind of reclaiming organic waste Rapid Thermal enzyme treater, can effectively process various organic wastes (as agricultural organic waste; City organic waste; Cultivation organic waste, food, butcher and biomass organic waste etc.).Although it is simple in structure that above-mentioned prior art has, easy to operate, be convenient to move, in production process, produce without waste residue, the gas of eliminating is mainly with water vapour and a small amount of CO
2be main, in fermentative production, by aerobic hot enzyme production technique, utilize thermophilic microbial inoculum, the fermentation time of organic solid waste can be shortened to 24 hours, feature rapidly and efficiently.But, also exist weak point.Above-mentioned prior art during the fermentation, along with material moisture constantly volatilizees, hot steam very easily on plane integral type top cover condensation become water droplet, water droplet accumulates to a certain degree, meeting secondary back, to reactor, causes the moisture of material to be difficult to volatilization, and moisture additional issue need increase energy consumption again.Meanwhile, the space of machine is relatively sealed, and circulation of air is limited, if cannot form as early as possible the free-running property structure of matter, the effect of aerobic fermentation process and efficiency will significantly reduce.In addition, leaf formula stirring rake in original equipment is also deposited some drawbacks in production fermentation, exist in aerobic fermentation process material turning insufficient, if there are foreign material to be easily stuck in the gap between blade and inwall in raw material, machine constantly stirs, can produce larger wearing and tearing to bucket wall, when serious, even under power effect, cause stirring rake distortion.After fermentation ends, when a large amount of discharging, discharging disc brake also easily stops up, and then causes blanking Efficiency Decreasing.The metal-coating of U-shaped reactor is still larger by the cylinder wall energy consumption of scattering and disappearing.
Based on some deficiency existing in above actual production process, further existing equipment is improved and upgraded.Be embodied in and change flat-top top cover into 1 group or several groups of ridge type top covers, reduce heat steam condensing at top cover.Meanwhile, introduce gas-fog separator, U-shaped reactor is connected with gas-fog separator, gas-fog separator is mainly used in industrial pipeline, and its groundwork principle is that a large amount of moisture steam enters steam separator, and moves with the centrifugal inclined that dips down therein; The moisture content of carrying secretly is because Speed Reduction is separated; Separated liquid flow through drain valve discharge, the steam of dry cleansing is discharged from separator outlet.Open gas-fog separator, can accelerate the efficiency of aerobic fermentation, collected and separated by the hot steam in reactor, can accelerate scattering and disappearing of material moisture, stop peculiar smell in reaction process, simultaneously capable of reducing energy consumption scatters and disappears, more obvious in the reaction later stage.Entirety fermentation time can have original 24 hours and foreshorten to 12-18 hour.Leaf formula stirring rake changes fist formula stirring rake into, can fine material stirring evenly can not brought to wearing and tearing to reactor inwall again.Along with improving constantly of industrial automation, pneumatic control valve is widely used, and in this equipment, can realize the accurate control of blanking, more efficient, easy to operate.
Summary of the invention
Goal of the invention: for the problem and shortage of above-mentioned existing existence, the object of this invention is to provide a kind of improvement reclaiming organic waste Rapid Thermal enzyme treater, overcome original reclaiming organic waste Rapid Thermal enzyme treater in the time utilizing fast organic solid waste composting, occur that in moisture evaporative process, easy secondary back causes; Aerobic insufficient in fermenting process; When in whipping process, easily wearing and tearing casing, blanking equivalent are large, efficiency is not high, the weak points such as energy consumption waste.The technical problem that the present invention also will solve is to provide a shock processing utilizing said apparatus to realize organic fertilizer production.
Technical scheme: for achieving the above object, the present invention is by the following technical solutions: a kind of improvement reclaiming organic waste Rapid Thermal enzyme treater, this device is by frame (1), U-shaped reactor, motor (3), wheel gearing (4), step-down gear (5), temperature housing (10) form, and its technical essential is:
1. the built-in oar hammerhead of reactor agitator, reactor outer wall is inlayed flexible electrical heating zone heating, sends out to answer and between still and body, fills the cotton packing of heating and thermal insulation cotton rock, and reactor top is made up of 1 group or the carinate top cover of a few block, and is provided with the viewing window of synthetic glass; At reactor top one middle side part and ridge top cover lower edge, to place air water separator by pipeline and ground and be connected, pneumatic control discharge gate is offered in the middle-end bottom of reactor.Whole reactor overcoat is filled the thick quality silicate composite thermo-insulating shaped material of 3-5cm, in order to insulation jacket.
2. the cover described in is ridge top cover, and top cover is provided with tubaeform opening for feed (14) and the venting port with filter screen (15) with plate, and is provided with the viewing window (16) of acrylic glass.
3. passing through at U-shaped reactor (2) top described in, placed gas-fog separator (8) by pipeline (21) and ground and is connected at an aerosol inlet mouth (19) and an aerosol air outlet (20).
4. the U-shaped reactor described in approaches top end two pairs of hair driers is installed, and according to setting formula timing to air blast in body, U-shaped reactor outer wall is inlayed the heating of flexible electrical hot-plate, answers for U-shaped and between still, hot plate and body, fills the cotton packing of heating and thermal insulation cotton rock.
5. welding or rivet 3-5 group tup type agitating vane (6) on the stir shaft at the U-shaped reactor middle part described in, every group of tup type agitating vane is made up of the tup of 3 different angles.
6. the transmission mechanism of the stirring described in is wheel gearing (4).
7. discharge gate device automatic discharging air valve switch (17) is offered in the middle-end bottom of the reactor described in.
8. the overcoat of the U-shaped reactor described in is filled the thick quality silicate composite thermo-insulating shaped material of 3-5cm, in order to insulation jacket (22).
Technical scheme of the present invention is below described in further detail:
A kind of improvement reclaiming organic waste Rapid Thermal enzyme treater, this device is by frame (1), U-shaped reactor (2), motor (3), wheel gearing (4), step-down gear (5), hammerhead agitating vane (6), reactor outer wall encapsulant layer (7), the outer steel plate (8) of U reactor, hot plate (9), temperature control (10), two pairs of hair driers (11), electrical control cabinet (12), 1 group or several groups of ridge type top covers (13), trumpet type opening for feed (14), venting port (15) with filter screen, acrylic glass window (16), automatic discharging air valve switch (17) and gas-fog separator (18) composition.Reactor top changes ridge type structure into by original flat-tope structure, ridge top cover is by 1 group or organize top cover more and form, on fixed roof one end (front view end), have 1 tubaeform opening for feed (14) and 3 venting port (15) with filter screen with plate, in a movable side, be provided with acrylic glass window (16), and can raise interpolation starter., be connected by pipeline (21) with gas-fog separator (18) by 1 aerosol inlet mouth (19) and 1 aerosol air outlet (20) at U-shaped reactor (2) top place, all reaction parameters are by electrical control cubicles (12) setup control or Artificial Control automatically.Automatic discharging air valve switch (17) is offered in the middle-end bottom of U-shaped reactor.The outer steel plate (8) of whole reactor is filled the thick quality silicate composite thermo-insulating shaped material of 3-5cm, in order to insulation jacket (22).It is characterized in that: above body frame, installing cross section is U-shaped reactor, the built-in tup type of reactor arm stirrer, reactor outer wall is inlayed the heating of flexible electrical heating zone, send out to answer and between still and body, fill the cotton packing of heating and thermal insulation cotton rock, reactor top is made up of 1 group or the carinate top cover of a few block, and is provided with the viewing window of synthetic glass; At reactor top one middle side part and ridge type top cover lower edge, to place gas-fog separator by pipeline and ground and be connected, whipping appts carries out transmission by wheel gearing, and pneumatic control discharge gate is offered in the middle-end bottom of reactor.Whole reactor overcoat is filled the thick quality silicate composite thermo-insulating shaped material of 3-5cm, in order to insulation jacket.
The present invention has advantages of:
Simple in structure, be easy to manufacture, handled easily and maintenance, high temperature is controlled, rotating speed is adjustable, mix, suitable microorganism enzymolysis quick fermentation shortens fermentation time on the basis of existing equipment, reduces production costs;
2. prepared fertilizer quality is high.Be suitable for family, community, factory, plant, restaurant etc. and process organic waste.
3. in production process, produce without waste residue, the gas of eliminating is mainly with water vapour and a small amount of CO
2be main, production process and the equal odorless of production product, free from extraneous odour produces, and with respect to the reclaiming organic waste Rapid Thermal enzyme treater of improveing, fermentation period is shorter, and whole fermentation time shortens to 12-18 hour.Stirring rake can not cause damage to reactor inwall, fermentation ends, and blanking is more rapidly and efficiently.
Brief description of the drawings
Fig. 1 is the reclaiming organic waste Rapid Thermal enzyme processor structure schematic diagram of improvement;
Fig. 2 is the left view of Fig. 1;
Fig. 3 is the right view of Fig. 1;
Fig. 4 is the vertical view of Fig. 1.
Accompanying drawing drawing explanation: be respectively frame (1), U-shaped reactor (2), motor (3), wheel gearing (4), step-down gear (5), hammerhead agitating vane (6), reactor outer wall encapsulant layer (7), the outer steel plate (8) of U reactor, hot plate (9), temperature control (10), two pairs of hair driers (11), electrical control cabinet (12), 1 group or several groups of ridge type top covers (13), trumpet type opening for feed (14), venting port (15) with filter screen, acrylic glass window (16), automatic discharging air valve switch (17), gas-fog separator (18), 1 aerosol inlet mouth (19), 1 aerosol air outlet (20), pipeline (21), insulation jacket (22) composition.
Embodiment
Below in conjunction with the drawings and specific embodiments, further illustrate the present invention, should understand these embodiment is only not used in and limits the scope of the invention for the present invention is described, after having read the present invention, those skilled in the art all fall within the application's claims limited range to the amendment of the various equivalent form of values of the present invention.
The first step: according to technical scheme, configure 22 assemblies and (refer to accompanying drawing 1, 2, 3, 4): be respectively frame (1), U-shaped reactor (2), motor (3), wheel gearing (4), step-down gear (5), hammerhead agitating vane (6), reactor outer wall encapsulant layer (7), the outer steel plate (8) of U reactor, hot plate (9), temperature control (10), two pairs of hair driers (11), electrical control cabinet (12), 1 group or several groups of ridge type top covers (13), trumpet type opening for feed (14), venting port (15) with filter screen, acrylic glass window (16), automatic discharging air valve switch (17), gas-fog separator (18), 1 aerosol inlet mouth (19), 1 aerosol air outlet (20), pipeline (21), insulation jacket (22) composition.
Second step: treater is by power section, heated for controlling temperature, stirring and speed regulation device, electric control gear, 1 group or several groups of ridge type top covers and gas-fog separator compositions and realize.
1, power section: variable-frequency motor, frequency transformer; Reduction box; Step-down gear; Step-down gear and motor mode of connection: geartransmission;
2, heating: directly adopt the heating of flexible electrical heating zone, Heating temperature≤120 DEG C, wear insulating cotton insulation outward;
3, stirring body: form is hammerhead, middle discharging, rotating speed is that 1-20rpm is adjustable;
4, automatic or people is controlled electric control box: stainless steel electric control box, and major function has: voltage, electric current show; Barrel temperature shows and electrical heating temperature shows and controls; Main frame opens, cuts out; The control of heating; Speed governing button;
5, sealing: the bearing seal at equipment two ends adopts opposite opened stuffing box, and filler is tetrafluoroethylene belt carcass packing.
6, U-shaped reactor is connected with gas-fog separator by pipeline; Discharge port is by Hysteresis for Pneumatic Control Valves;
7, equipment material: except step-down gear, motor, air water separator, eaves formula top cover, bearing, gear, miscellaneous part all adopts 304 stainless steel processing, also can adopt corrosion preventing steel plate;
8, security measures: bearing end and step-down gear end all sites are joined stainless steel case.
The 3rd step: according to reactor front and construction profile, assembling and welding instrument, gummed, weld is seamless polishing.
Stainless steel surfaces externally and internally is polished to 100 orders; After steel surface rust cleaning, be coated with twice epoxy finish.
As shown in Fig. 1～4, a kind of improvement reclaiming organic waste Rapid Thermal enzyme treater, comprises frame, reactor, change speed motor, wheel gearing, step-down gear, temperature control, the two pairs of hair driers, electrical control cabinet, 1 group or several groups of ridge type top covers and air water separator composition.It is characterized in that: above body frame, installing cross section is U-shaped reactor, the built-in oar hammerhead of reactor agitator, reactor outer wall is inlayed the heating of flexible electrical heating zone, send out to answer and between still and body, fill the cotton packing of heating and thermal insulation cotton rock, reactor top is made up of 1 group or the carinate top cover of a few block, and is provided with the viewing window of synthetic glass; At reactor top one middle side part and ridge type top cover lower edge, to place air water separator by pipeline and ground and be connected, pneumatic control discharge gate is offered in the middle-end bottom of reactor.Whole reactor overcoat is filled the thick quality silicate composite thermo-insulating shaped material of 3-5cm, in order to insulation jacket.
Treater is by power section, heated for controlling temperature, stirring and speed regulation device, electric control gear, 2 groups or several groups of ridge type top covers and gas-fog separator compositions and realize.Mainly formed by 22 construction packages, respectively: be respectively frame (1), U-shaped reactor (2), motor (3), wheel gearing (4), step-down gear (5), hammerhead agitating vane (6), reactor outer wall encapsulant layer (7), the outer steel plate (8) of U reactor, hot plate (9), temperature control (10), two pairs of hair driers (11), electrical control cabinet (12), 1 group or several groups of ridge type top covers (13), trumpet type opening for feed (14), venting port (15) with filter screen, acrylic glass window (16), automatic discharging air valve switch (17), gas-fog separator (18), 1 aerosol inlet mouth (19), 1 aerosol air outlet (20), pipeline (21), insulation jacket (22) composition.Specifically introduce effect of the present invention by 4 embodiment below:
embodiment 1
Pilot scale stirring reactor is produced fertilizer (not adding steam separator) taking single manioc waste as fermenting raw materials.
Taking manioc waste as raw material, utilize microbial inoculum BM1, manioc waste fertilizer is prepared in fermentation.
Manioc waste moisture: 75.25%, weight in wet base: 80kg, 0.5 ‰ BM1 addition: 40g
Production technique: in stirring reactor, fermentation reaction temperature is 80-85 DEG C, ventilatory frequency, for opening 10 minutes, stops 50 minutes, and mixing speed is 3 r/min.
Whole fermentation time is 24 hours, material 35.6kg, and moisture is 31.25%.
embodiment 2
Pilot scale stirring reactor is produced fertilizer (adding steam separator) taking single manioc waste as fermenting raw materials.
Taking manioc waste as raw material, utilize microbial inoculum BM1, manioc waste fertilizer is prepared in fermentation.
Manioc waste moisture: 75.25%, weight in wet base: 80kg, 0.5 ‰ BM1 addition: 40g
Production technique: in stirring reactor, fermentation reaction temperature is 80-85 DEG C, ventilatory frequency, for opening 10 minutes, stops 50 minutes, and mixing speed is 3 r/min, adds carbonated drink separating device.
Whole fermentation time is 18 hours, the heavy 34.78kg of material, and moisture is 28.25 %.Collect moisture 45.63kg.
embodiment 3
Pilot scale stirring reactor is produced fertilizer (not adding steam separator) taking manioc waste and stalk as fermenting raw materials.
Taking manioc waste as raw material, utilize microbial inoculum BM1, manioc waste fertilizer is prepared in fermentation.
Manioc waste moisture: 75.25%, stalk moisture: 8.35%, manioc waste weight: 70kg, straw powder: 10kg, 1 ‰ BM1 addition: 80g
Production technique: in stirring reactor, fermentation reaction temperature is 80-85 DEG C, ventilatory frequency, for opening 10 minutes, stops 50 minutes, and mixing speed is 3 r/min, adds carbonated drink separating device.
Whole fermentation time is 21 hours, the heavy 32.33kg of material, and moisture is 29.03 %.
embodiment 4
Pilot scale stirring reactor is produced fertilizer (adding steam separator) taking manioc waste and stalk as fermenting raw materials.
Taking manioc waste as raw material, utilize microbial inoculum BM1, manioc waste fertilizer is prepared in fermentation.
Manioc waste moisture: 75.25%, stalk moisture: 8.35%, manioc waste weight: 70kg, straw powder: 10kg, 1 ‰ BM1 addition: 80g
Production technique: in stirring reactor, fermentation reaction temperature is 80-85 DEG C, ventilatory frequency, for opening 10 minutes, stops 50 minutes, and mixing speed is 3 r/min, adds carbonated drink separating device.
Whole fermentation time is 16 hours, the heavy 33.21kg of material, and moisture is 27.13 %.Collect moisture 42.35kg.
embodiment 5
To process 15 tons of equipment 22000L day, add the manioc waste of moisture 57.01%, 12.5 tons, add 12.5 kilograms of starter BM1, parameter setting is respectively jacket temperature: 120-145 DEG C, initial setting temperature of charge: 70-85 DEG C; Rotating speed: 3rpm, blowing frequency: open 10min, stop 50min.Operation hours 23.5 hours, 6.5 tons of dischargings.
embodiment 6
To process 15 tons of equipment 22000L day, adopt aerosol junctor, add the manioc waste of moisture 55.01%, 12.5 tons, add 12.5 kilograms of starter BM1, parameter setting is respectively jacket temperature: 120-145 DEG C, initial setting temperature of charge: 70-85 DEG C; Rotating speed: 3rpm, blowing frequency: open 10min, stop 30min.Operation hours 17.5 hours, 6.7 tons of dischargings.
Claims (8)
1. an improvement reclaiming organic waste Rapid Thermal enzyme treater, this device is by frame (1), U-shaped reactor, motor (3), wheel gearing (4), step-down gear (5), temperature housing (10) form, it is characterized in that: the built-in oar hammerhead of reactor agitator, reactor outer wall is inlayed the heating of flexible electrical heating zone, send out to answer and between still and body, fill the cotton packing of heating and thermal insulation cotton rock, reactor top is made up of 1 group or the carinate top cover of a few block, and is provided with the viewing window of synthetic glass; Reactor top one middle side part and ridge top cover lower edge, place air water separator by pipeline and ground and be connected, and pneumatic control discharge gate is offered in the middle-end bottom of reactor; Whole reactor overcoat is filled the thick quality silicate composite thermo-insulating shaped material of 3-5cm, in order to insulation jacket.
2. a kind of improvement reclaiming organic waste Rapid Thermal enzyme treater according to claim 1, it is characterized in that, described cover is ridge top cover, top cover is provided with tubaeform opening for feed (14) and the venting port with filter screen (15) with plate, and is provided with the viewing window (16) of acrylic glass.
3. a kind of improvement reclaiming organic waste Rapid Thermal enzyme treater according to claim 1, it is characterized in that, described at U-shaped reactor (2) top by an aerosol inlet mouth (19) and an aerosol air outlet (20), be connected by pipeline (21) and ground placement gas-fog separator (8).
4. a kind of improvement reclaiming organic waste Rapid Thermal enzyme treater according to claim 1, it is characterized in that, described U-shaped reactor approaches top end two pairs of hair driers is installed, according to setting formula timing to air blast in body, U-shaped reactor outer wall is inlayed flexible electrical hot-plate heating, answers for U-shaped and between still, hot plate and body, fills the cotton packing of heating and thermal insulation cotton rock.
5. a kind of improvement reclaiming organic waste Rapid Thermal enzyme treater according to claim 1, it is characterized in that, welding or rivet 3-5 group tup type agitating vane (6) on the stir shaft at described U-shaped reactor middle part, every group of tup type agitating vane is made up of the tup of 3 different angles.
6. a kind of improvement reclaiming organic waste Rapid Thermal enzyme treater according to claim 1, is characterized in that, the transmission mechanism of described stirring is wheel gearing (4).
7. a kind of improvement reclaiming organic waste Rapid Thermal enzyme treater according to claim 1, is characterized in that, discharge gate device automatic discharging air valve switch (17) is offered in the middle-end bottom of described reactor.
8. a kind of improvement reclaiming organic waste Rapid Thermal enzyme treater according to claim 1, is characterized in that, the overcoat of described U-shaped reactor is filled the thick quality silicate composite thermo-insulating shaped material of 3-5cm, in order to insulation jacket (22).
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| Application Number | Priority Date | Filing Date | Title |
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| CN201410239925.1A CN104163667A (en) | 2014-05-30 | 2014-05-30 | Improved rapid thermal enzyme treating device for recycling organic waste |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201410239925.1A CN104163667A (en) | 2014-05-30 | 2014-05-30 | Improved rapid thermal enzyme treating device for recycling organic waste |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2811293Y (en) * | 2005-08-12 | 2006-08-30 | 天津市三英新技术发展有限公司 | Automatic biochemical treatment system device for kitchen swilling |
| CN201999866U (en) * | 2011-02-14 | 2011-10-05 | 林柏鸿 | High-speed fermented organic waste disposer |
| CN203319883U (en) * | 2013-06-06 | 2013-12-04 | 刘立鹤 | Recycled rapid thermal enzyme treating device of organic waste |
| CN103524167A (en) * | 2013-10-08 | 2014-01-22 | 陈志坚 | Energy-saving drainage device of livestock and poultry culturing farm organic waste processor |
| CN203432384U (en) * | 2013-07-09 | 2014-02-12 | 张维民 | Vapor condensation water segregator in microorganism kitchen waste disposer |
| CN203498272U (en) * | 2013-09-12 | 2014-03-26 | 宁波高德威机械科技有限公司 | Organic waste processor |
-
2014
- 2014-05-30 CN CN201410239925.1A patent/CN104163667A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2811293Y (en) * | 2005-08-12 | 2006-08-30 | 天津市三英新技术发展有限公司 | Automatic biochemical treatment system device for kitchen swilling |
| CN201999866U (en) * | 2011-02-14 | 2011-10-05 | 林柏鸿 | High-speed fermented organic waste disposer |
| CN203319883U (en) * | 2013-06-06 | 2013-12-04 | 刘立鹤 | Recycled rapid thermal enzyme treating device of organic waste |
| CN203432384U (en) * | 2013-07-09 | 2014-02-12 | 张维民 | Vapor condensation water segregator in microorganism kitchen waste disposer |
| CN203498272U (en) * | 2013-09-12 | 2014-03-26 | 宁波高德威机械科技有限公司 | Organic waste processor |
| CN103524167A (en) * | 2013-10-08 | 2014-01-22 | 陈志坚 | Energy-saving drainage device of livestock and poultry culturing farm organic waste processor |
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Application publication date: 20141126 |
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