CN203124393U - Biochemical fermentation device - Google Patents

Biochemical fermentation device Download PDF

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Publication number
CN203124393U
CN203124393U CN2013200551166U CN201320055116U CN203124393U CN 203124393 U CN203124393 U CN 203124393U CN 2013200551166 U CN2013200551166 U CN 2013200551166U CN 201320055116 U CN201320055116 U CN 201320055116U CN 203124393 U CN203124393 U CN 203124393U
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CN
China
Prior art keywords
fermentation device
fermentation
main
ribbon
main fermentation
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Withdrawn - After Issue
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CN2013200551166U
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Chinese (zh)
Inventor
许文姬
李国声
李汉声
李振声
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Southern China Renewable Resources (zhongshan) Co Ltd
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Southern China Renewable Resources (zhongshan) Co Ltd
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Priority to CN2013200551166U priority Critical patent/CN203124393U/en
Priority to HK13108025A priority patent/HK1180892A2/en
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Publication of CN203124393U publication Critical patent/CN203124393U/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B5/00Operations not covered by a single other subclass or by a single other group in this subclass
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/02Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • C10L1/026Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression ignition
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L5/00Solid fuels
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • C10L5/48Solid fuels essentially based on materials of non-mineral origin on industrial residues and waste materials
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • 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
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

Abstract

The utility model provides a biochemical fermentation device. The fermentation device comprises an anaerobic fermentation tank and a main fermentation device, wherein the main fermentation device comprises two secondary fermenting devices and more than one main fermentation device, wherein the two secondary fermenting devices are arranged above the main fermentation device; feeding openings are arranged at connection parts of the secondary fermenting devices and the main fermentation device; the main fermentation device is externally provided with a material elevator for inputting materials into the secondary fermenting devices; the secondary fermenting devices are integrally provided with agitation equipment; the main fermentation device is internally provided with a double-layered screw belt agitator; the anaerobic fermentation tank is connected with the main fermentation device; and the anaerobic fermentation tank is used for adding the materials into the main fermentation device through an automatic discharging system. A biochemical fermentation method comprises the following steps of: A, simultaneously generating pre-fermented materials in the anaerobic fermentation tank and the two secondary fermenting devices; B, conveying the materials in the secondary fermenting devices into the main fermentation device through automatic conveying equipment and conveying the materials in the anaerobic fermentation tank into the main fermentation device to carry out secondary fermentation; and C, after the secondary fermentation is finished, carrying out discharging.

Description

A kind of biochemical fermentation device
Technical field
The utility model discloses a kind of changing food waste treating apparatus, more specifically relates to the biochemical fermentation device of using in a kind of changing food waste.
Background technology
The science and technology of utilization of waste as resource; through using for a long time; proved a reason; if be exactly the single application of resource treatment technique of discarded object; its consequence will be brought bigger crisis to environment for human survival; especially the serious problems that produce secondary pollution are difficult to control, so the integrated treatment of discarded object has become the trend of current development.The composition of changing food waste is extremely complicated, wherein comprises materials such as sewage, polybag, plastic bottle, useless cloth, putrefactive organism, paper, metal Bottle ﹠ Can, broken glass, broken potsherd, animal fat, vegetable fat, primary bacterial body.At present the changing food waste into resources treatment technology at home and abroad method and technology in present " a hundred flowers blossom " situation, but substantially all be simple single-item handling, the international environmental protection treatment trend and direction that does not have trend to turn to integrated treatment, utilize and dispose from simple processing, may cause inevitable attachment in the changing food waste to shift and disorderly fill out and leave about, cause water and soil to pollute, or shift, not only stop up the urban sewage pipeline, distribute foul odour, cause serious secondary pollution.The single treatment process of changing food waste is worth to consider it is feasible from recycling, but considers from the environment of preserving our planet for a long time, the people's comprehensive angle livable, the protection atmospheric environment, still may be more harm than good.In the changing food waste processing procedure, need use the biochemical fermentation method changing food waste is handled, present biochemical fermentation device and the method mechanism of employing are unreasonable, and treatment effect is bad.
Summary of the invention
At the above-mentioned bad shortcoming of mentioning of changing food waste biochemical fermentation effect of the prior art, the utility model provides a kind of new biochemical fermentation device, it adopts the method for anaerobic fermentation and aerobic fermentation combined ferment, and by main fermentation device and side fermentation device two-step fermentation, realize the effect of automatic biochemical fermentation.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of biochemical fermentation device, installation for fermenting comprises anaerobic fermentation pond and main fermentation device, described main fermentation device comprises two side fermentation devices and more than one main fermentation device, two side fermentation devices are arranged on main fermentation device top, side fermentation device and main fermentation device junction are provided with charging aperture, main fermentation device peripheral hardware is useful on material is inputed to material elevator in the side fermentation device, be provided with mixing plant in the side fermentation device, be provided with double-deck helical ribbon agitator in the main fermentation device, the anaerobic fermentation pond is connected with the main fermentation device, and drop into material in the main fermentation device by automatic discharge system in the anaerobic fermentation pond.
The technical scheme that its technical problem that solves the utility model adopts further comprises:
Described double-deck helical ribbon agitator comprises axis body, internal layer ribbon and outside ribbon, the internal layer ribbon is arranged on outer ribbon inside, internal layer ribbon and outer ribbon are all banded twist, and be fixedly mounted on the axis body respectively, the hand of spiral of internal layer ribbon and outer ribbon is opposite, and the axis body periphery of double-deck helical ribbon agitator installs the ploughshare blade additional.
Be a main shaft in the middle of the described mixing plant, be installed with more than one stirring vane on the axis.
The top is provided with the material that can move automatically and stirs blanking device in the described anaerobic fermentation pond, and material stirs blanking device and connects automatic feeding funnel by the ribbon conveyer.
The beneficial effects of the utility model are: adopt the method for anaerobic fermentation and aerobic fermentation combined ferment in the utility model, and by main fermentation device and side fermentation device two-step fermentation, realize the effect of automatic biochemical fermentation, simple and reasonable for structure, ferment effect is good.
Below in conjunction with the drawings and specific embodiments the utility model is described further.
Description of drawings
Fig. 1 the utility model structural representation.
Fig. 2 is the utility model main fermentation device cross-sectional view.
Fig. 3 is the utility model perspective view.
Among the figure, 1-material elevator, 2-anaerobic fermentation pond, 3-seal cover, the automatic discharge system of 4-, 5-material automatic blanking agitator, the 5A-automatic feeding funnel, the 6-bacterial classification activates the pond, 7-main fermentation device, 8-side fermentation device, 9-mixing plant, the 10-automatic conveying equipment, 11-horizontal type shell, 12-supporting, the 13-conduction oil is carried comb, the double-deck helical ribbon agitator of 14-, 15-ploughshare blade, the 16-motor, 17-speed changer, 18-gear, the 19-chain, 20-charging aperture, 21-operated pneumatic valve, the 22-observation window, the 23-air is defeated, comb, 24-material sample tap, 25-self-emptying hole, 26-automatic valve lock, 27-exhaust outlet, the 28-air-introduced machine, 29-automatic cover-turning device, 30-discharging opening.
The specific embodiment
Present embodiment is the utility model preferred embodiment, and other all its principles are identical with present embodiment or approximate with basic structure, all within the utility model protection domain.
Please referring to accompanying drawing 1 and accompanying drawing 3, in the utility model, the biochemical fermentation device is mainly used in changing food waste is carried out biochemical treatment, and the biochemical fermentation device mainly comprises some anaerobic fermentation pond 2 and main fermentation devices 8 compositions of uniting use mutually, is respectively anaerobic fermentation and aerobic fermentation.Be provided with anaerobic fermentation pond 2 in the anaerobic ferment process, anaerobic fermentation pond 2 is cylindric, the top is provided with seal cover 3, seal cover 3 is by pneumatic tool (being automatic cover-turning device 29) control folding, in the present embodiment, automatic cover-turning device 29 is connected seal cover 3 tops by connecting rod, promotes link motion by cylinder, realizes folding by connecting rod pulling seal cover 3.Anaerobic fermentation pond 2 inner bottom parts are equipped with automatic discharge system 4, automatically discharge system 4 in a tubular form, inside is provided with spiral stirring blade, the top is provided with the material agitator 5 that can move automatically in the anaerobic fermentation pond 2, one side in anaerobic fermentation pond 2 arranges bacterial classification and activates pond 6, bacterial classification activates 6 sides, pond and is provided with discharging opening 30, and discharging opening 30 is communicated with automatic discharge system 4.In the present embodiment, anaerobic fermentation workshop section is provided with several anaerobic fermentation ponds of uniting use mutually, and one of them activates pond 6 for bacterial classification.
Please in conjunction with referring to accompanying drawing 2, the main fermentation device is divided into two side fermentation devices 8 and more than one main fermentation device constitutes jointly, and in the present embodiment, is provided with material elevator 1, and material elevator 1 is used for changing food waste is upwards promoted, and drops in one of them side fermentation device.Two side fermentation devices 8 are installed on main fermentation device top, be provided with material conveying pipe between the major-minor fermentor, this conveyance conduit is the automatic conveying equipment 10 of being located at side fermentation device 8 bottoms, in the present embodiment, automatic conveying equipment 10 is cylindric, be provided with spiral stirring blade in the cylinder-like shell, through automatic conveying equipment 10 material is sent into the main fermentation device, side fermentation device 8 outlets simultaneously and the middle operated pneumatic valve 21 that is equipped with of the interface channel of main fermentation device import, in the present embodiment, be equipped with in side fermentation device 8 and rub the mixing plant 9 that stirs work with the hands, mixing plant 9 is middle main shaft, be installed with a plurality of stirring vanes on the axis, be used for material is stirred.In the present embodiment, offer exhaust outlet 27 on the housing top of side fermentation device 8, connect air-introduced machine 28 on the exhaust outlet 27, the gas that is used for producing in the side fermentation device 8 is discharged.The main fermentation device mainly contains horizontal type shell 11, supporting 12, conduction oil carries comb 13 and double-deck helical ribbon agitator 14 to form, in the present embodiment, double-deck helical ribbon agitator 14 has axis body, internal layer ribbon and outside ribbon are formed, the internal layer ribbon is arranged on outer ribbon inside, internal layer ribbon and outer ribbon are all banded twist, and be fixedly mounted on the axis body respectively, the hand of spiral of internal layer ribbon and outer ribbon is opposite, the axis body periphery of double-deck helical ribbon agitator 14 installs ploughshare blade 15 additional, transmission system in the present embodiment comprises motor 16, speed changer 17, gear 18 and chain 19, gear 18 and chain 19 are separately positioned on the two ends in horizontal type shell 11 outsides, speed changer 17 is provided with a plurality of, concrete quantity can be set according to actual needs, in the present embodiment, be provided with three, motor 16 directly drives basic transmission, basic transmission drives two from speed changer by power transmission shaft, each is equipped with a driving gear 18 from speed changer, the axis body two ends of double-deck helical ribbon agitator 14 are separately installed with a driven gear, two driving gears 18 are connected on the driven gear by chain 19 respectively, drive double-deck helical ribbon agitator 14 and rotate.In the present embodiment, main fermentation device top offers charging aperture 20, and operated pneumatic valve 21 is equipped with at charging aperture 20 places.Observation window 22 is installed in position, middle and upper part, horizontal type shell 11 side, be used for watching the response situation in the horizontal type shell 11, position, middle and upper part, horizontal type shell 11 side is separately installed with also that air is defeated, comb 23 and material sample tap 24, air is defeated, comb 23 is used for discharging to horizontal type shell 11 interior bubbling airs or with horizontal type shell 11 internal gas, and material sample tap 24 is used for the material in the horizontal type shell 11 is taken a sample.Self-emptying hole 25 is offered in horizontal type shell 11 bottoms, and automatic valve lock 26 is equipped with at 25 places, self-emptying hole, is used for discharging.In the present embodiment, at the main fermentation device exhaust outlet (not drawing among the figure) is housed also.
In the utility model, auto temperature controlled system is installed also in the biochemical device.
Carry out the method for biochemical fermentation by said apparatus, comprise the steps:
1, at first act on simultaneously by anaerobic fermentation pond 2 and two side fermentation devices 8, generate pre-fermentation materials:
1-1, anaerobic fermentation pond 2 fermentations: biochemical treatment is carried out in the pulverizing of solid base material and adding bacterial classification, in the utility model, selection for solid base, it at first is the normality crops tangerine stalk of considering changing food waste treatment plant neighboring area, in the present embodiment, get beans kind crop tangerine stalk (as: soya bean, mung bean, in red bean and the pea one or more) account for 50% of total fermentation base-material weight---80%, other gets grass tree material crop (as: wheat, corn, millet, paddy rice) this season tangerine stalk accounts for 20% of total fermentation base-material weight---and 50%, in the present embodiment, both weight ratios of arranging in pairs or groups are 60%:40%, the tangerine stalk of above-mentioned two kinds of types is arranged in pairs or groups as compound, select for use the reason of this hybrid solid base-material to be: legume tangerine stalk protein content height, but solubility sugar content is low, not high at fermentation initial stage microbial activity, and the nutritive value of grass tree material crop material own is not high, but solubility sugar content height, these two section's class crop tangerine stalks are mixed, not only can improve fermented quality, and the nutriment of this two classes crop tangerine stalk is replenished mutually; It is 0.5mm that mixed material is broken into particle diameter---the powder of 1mm, and add and to decompose coarse-fibred composite bacteria agent capable the said mixture material is carried out biochemical treatment, bacterial classification is no less than two kinds in the composite bacteria agent capable of indication, wherein a kind of is aspergillus oryzae, the input amount of composite bacteria agent capable is 1% of hybrid solid base-material, and adds chemical analysis calcium oxide, sodium chloride, dibastic sodium phosphate and urea;
1-2, main fermentation device 7 are made up of two main fermentation devices and two side fermentation devices, and at first two side fermentation devices are fermented to material in advance by multiple different strain respectively.At first having added manually in one of them side fermentation device 8, the changing food waste of deactivation is base-material, add and account for base-material weight 8%---10% wheat bran, accounting for base-material weight 10%---15% rice bran and the white sugar that accounts for base-material weight 1% join in the broken base-material behind the furnishing pasty state as compound, the bacterial classification that adds 2-3% again, fermentation process adopts old method fermentation method, and (Fa Jiao bacterial classification is Saccharomyces cerevisiae first, addition is 2% of total fermentation base-material weight---3%, 1% brown sugar of the base-material weight of fermenting again, mixes also the furnishing pasty state with broken base-material after, be heated to 24 ℃---25 ℃, add Saccharomyces cerevisiae again), and utilize the deal with the work thermal source of other workshop sections of changing food waste to produce, and fully stir, enhanced aeration, strengthening yeast growth, stop to stir and aeration to send out the standing for fermentation time be 12 hours.In the present embodiment, the old ferment method of indication is after each fermentation is finished, when discharging, preserve total material 10% as fermentation next time masterbatch, the Saccharomyces cerevisiae addition of later each fermentation can reduce, and only needs to add 60% of bacterial classification weight that fermentation first adds.
1-3, another side fermentation device 8 are the pre-fermentor of main material, and adopting the changing food waste that has also dewatered through artificial deactivation, cleaning is that base-material carries out solid state fermentation.The bacterial classification selected for use of this stage is by Trichoderma viride, candida tropicalis bacterium, bacterium and Endomycopsis Fibnligera saccharomycete are formed four bacterium mix bacterium agents in vain, the part by weight of four bacterium is 2:2:1:1, inoculum concentration (being the input amount of mix bacterium agent) is 2% of gross weight, add simultaneously and account for gross weight 1%---1.5% urea, temperature is 25 ℃---30 ℃ for good, the highlyest be no more than 42 ℃, per hour rolled once by automatic equipment, fermentation time 9 hours---10 hours, ventilation condition is that 8min/h(namely per hour ventilated 8 minutes), ventilation is 0.2m 3/ h.The thermal source of this pre-fermentation workshop section is provided by the changing food waste waste heat that the thermal source of other workshop sections produces of dealing with the work.In the present embodiment, Trichoderma viride in the bacterial classification cooperates bacterium in vain that the reduction of the crude fiber content in the changing food waste is played effect extremely significantly, and candida tropicalis, bacterium, Trichoderma viride reach obvious level to the raising effect of thick protein and true protein in vain, intend the endomyces saccharomycete as auxiliary mould.
2, material inoculation namely after the pre-workshop section of fermenting finishes, with the material of two side fermentation devices, is sent main biochemical device to by the automatic conveying equipment 10 of being located at the fermentor bottom and is carried out secondary fermentation.
The material input main fermentation device of pre-biochemical treatment will be carried out, wherein the processing in the main fermentation device comprises: the material in stalk fermentation material and the pre-biochemical treatment apparatus is imported the main fermentation device in the main biochemical device, the input ratio of material is: in the stalk fermentation material 10% of total weight of material percentage---40%, the Saccharomyces cerevisiae fermentation materials accounts for 20% of total weight of material percentage, the fermentation materials of the second pre-biochemical treatment accounts for 40% of total weight of material percentage---and 70%, after three kinds of materials after pre-fermentation process enter in the main fermentation device, double-deck helical ribbon agitator 14 is done 360 degree rotations under the driving of power source, rotating speed is 6-9 commentaries on classics/min, spinning movement is travel directions, material is made low speed slowly to be stirred, temperature in the main fermentation device begins warm from initial 20 ℃, it is 28 ℃ with temperature increase progressively, constant temperature time is to close air valve 23 after 4 hours, temperature raising to 35 simultaneously ℃---38 ℃, behind the constant temperature time 3 hours, open air bleeding valve, utilize the malleation in the main biochemical device, moisture content is discharged, after above-mentioned secondary constant temperature time is finished, temperature raising to 82 ℃ again, time is 2 hours, after all finishing whole secondary fermentation operation, open blower unit 28 air drafts, the aqueous vapor in this moment fermentation materials will enter gas and water separator and the air environment-friendly processing unit is handled (not being part of the present utility model) with exhaust system.The whole secondary fermentation time amounts to 9 hours, and this working time will finish fast from microbial reproduction and summit of growth phase and dormancy or dead overall process.The oxygen-supplying amount that this zymotechnique needs is less relatively, its oxygen branch derives between the space and specific area between the dehydrated material, and energy consumption is less, the time is shorter, avoided microorganism utilization carbon skeleton wherein as the energy effectively, and the problem of the economic worth of class is raised in the influence of the excitant ammonia that dehydrogenation simultaneously produces flavor;
3, discharging.
Adopt the method for anaerobic fermentation and aerobic fermentation combined ferment in the utility model, and by main fermentation device and side fermentation device two-step fermentation, realize the effect of automatic biochemical fermentation, simple and reasonable for structure, ferment effect is good.

Claims (4)

1. biochemical fermentation device, it is characterized in that: described installation for fermenting comprises anaerobic fermentation pond (2) and main fermentation device (7), described main fermentation device (7) comprises two side fermentation devices (8) and more than one main fermentation device, two side fermentation devices (8) are arranged on main fermentation device top, side fermentation device (8) is provided with charging aperture (20) with main fermentation device junction, main fermentation device peripheral hardware is useful on material is inputed to the interior material elevator (1) of side fermentation device (8), be provided with mixing plant (9) in the side fermentation device (8), be provided with double-deck helical ribbon agitator (14) in the main fermentation device, anaerobic fermentation pond (2) is connected with the main fermentation device, and drop into material in the main fermentation device by automatic discharge system (4) anaerobic fermentation pond (2).
2. biochemical fermentation device according to claim 1, it is characterized in that: described double-deck helical ribbon agitator (14) comprises axis body, internal layer ribbon and outside ribbon, the internal layer ribbon is arranged on outer ribbon inside, internal layer ribbon and outer ribbon are all banded twist, and be fixedly mounted on the axis body respectively, the hand of spiral of internal layer ribbon and outer ribbon is opposite, and the axis body periphery of double-deck helical ribbon agitator (14) installs ploughshare blade (15) additional.
3. biochemical fermentation device according to claim 1 and 2 is characterized in that: be a main shaft in the middle of the described mixing plant (9), be installed with more than one stirring vane on the axis.
4. biochemical fermentation device according to claim 1 and 2, it is characterized in that: the top is provided with the material that can move automatically and stirs blanking device (5) in the described anaerobic fermentation pond (2), and material stirs blanking device and connects automatic feeding funnel (5A) by the ribbon conveyer.
CN2013200551166U 2012-11-23 2013-01-31 Biochemical fermentation device Withdrawn - After Issue CN203124393U (en)

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Application Number Priority Date Filing Date Title
CN2013200551166U CN203124393U (en) 2012-11-23 2013-01-31 Biochemical fermentation device
HK13108025A HK1180892A2 (en) 2013-01-31 2013-07-09 A biochemical fermentation device

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CN201210481274 2012-11-23
CN201210481274.8 2012-11-23
CN2013200551166U CN203124393U (en) 2012-11-23 2013-01-31 Biochemical fermentation device

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CN203124393U true CN203124393U (en) 2013-08-14

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CN2013200551166U Withdrawn - After Issue CN203124393U (en) 2012-11-23 2013-01-31 Biochemical fermentation device
CN201310038171.9A Expired - Fee Related CN103084049B (en) 2012-11-23 2013-01-31 Plasma photocatalyst anion air deodorization, sterilizing unit
CN201320054411XU Withdrawn - After Issue CN203316248U (en) 2012-11-23 2013-01-31 Combined screening system for kitchen waste
CN201310038252.9A Expired - Fee Related CN103071666B (en) 2012-11-23 2013-01-31 Integrated equipment for omnibearing treatment of kitchen garbage and production method of products
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CN201310038148.XA Expired - Fee Related CN103056151B (en) 2012-11-23 2013-01-31 Kitchen waste oxidizing, deodorizing, inactivating, washing and salt-reducing device
CN201310037944.1A Expired - Fee Related CN103056022B (en) 2012-11-23 2013-01-31 Combined screening system of kitchen wastes
CN201310038136.7A Expired - Fee Related CN103115477B (en) 2012-11-23 2013-01-31 Automatic discharging multi-stage drying device
CN201310038186.5A Expired - Fee Related CN103056152B (en) 2012-11-23 2013-01-31 biochemical fermentation method and device
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CN2013200551768U Expired - Fee Related CN203124394U (en) 2012-11-23 2013-01-31 Material selecting device
CN2013200552991U Withdrawn - After Issue CN203124395U (en) 2012-11-23 2013-01-31 Oxidization, deodorization, inactivation, cleaning and desaltation device for kitchen waste
CN2013200551753U Withdrawn - After Issue CN203323492U (en) 2012-11-23 2013-01-31 Automatic discharge multi-stage drying device
CN201310038156.4A Expired - Fee Related CN103074131B (en) 2012-11-23 2013-01-31 Preparation method and device of oxygen-enriched microemulsion mixed biodiesel
CN2013200542519U Withdrawn - After Issue CN203124392U (en) 2012-11-23 2013-01-31 Integrated equipment for comprehensive treatment of kitchen waste
CN201310038212.4A Expired - Fee Related CN103060100B (en) 2012-11-23 2013-01-31 Distillation-free biodiesel production method and system
CN201310038166.8A Expired - Fee Related CN103055650B (en) 2012-11-23 2013-01-31 Exhaust treatment system

Family Applications After (16)

Application Number Title Priority Date Filing Date
CN201310038171.9A Expired - Fee Related CN103084049B (en) 2012-11-23 2013-01-31 Plasma photocatalyst anion air deodorization, sterilizing unit
CN201320054411XU Withdrawn - After Issue CN203316248U (en) 2012-11-23 2013-01-31 Combined screening system for kitchen waste
CN201310038252.9A Expired - Fee Related CN103071666B (en) 2012-11-23 2013-01-31 Integrated equipment for omnibearing treatment of kitchen garbage and production method of products
CN201310037324.8A Expired - Fee Related CN103072726B (en) 2012-11-23 2013-01-31 Plastic bag segmenting and lacerating device for holding kitchen wastes
CN201310038148.XA Expired - Fee Related CN103056151B (en) 2012-11-23 2013-01-31 Kitchen waste oxidizing, deodorizing, inactivating, washing and salt-reducing device
CN201310037944.1A Expired - Fee Related CN103056022B (en) 2012-11-23 2013-01-31 Combined screening system of kitchen wastes
CN201310038136.7A Expired - Fee Related CN103115477B (en) 2012-11-23 2013-01-31 Automatic discharging multi-stage drying device
CN201310038186.5A Expired - Fee Related CN103056152B (en) 2012-11-23 2013-01-31 biochemical fermentation method and device
CN2013200551772U Expired - Fee Related CN203128526U (en) 2012-11-23 2013-01-31 Distillation-free biodiesel production system
CN2013200551768U Expired - Fee Related CN203124394U (en) 2012-11-23 2013-01-31 Material selecting device
CN2013200552991U Withdrawn - After Issue CN203124395U (en) 2012-11-23 2013-01-31 Oxidization, deodorization, inactivation, cleaning and desaltation device for kitchen waste
CN2013200551753U Withdrawn - After Issue CN203323492U (en) 2012-11-23 2013-01-31 Automatic discharge multi-stage drying device
CN201310038156.4A Expired - Fee Related CN103074131B (en) 2012-11-23 2013-01-31 Preparation method and device of oxygen-enriched microemulsion mixed biodiesel
CN2013200542519U Withdrawn - After Issue CN203124392U (en) 2012-11-23 2013-01-31 Integrated equipment for comprehensive treatment of kitchen waste
CN201310038212.4A Expired - Fee Related CN103060100B (en) 2012-11-23 2013-01-31 Distillation-free biodiesel production method and system
CN201310038166.8A Expired - Fee Related CN103055650B (en) 2012-11-23 2013-01-31 Exhaust treatment system

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KR (1) KR20150105299A (en)
CN (17) CN203124393U (en)
HK (9) HK1180713A1 (en)
RU (1) RU2015123832A (en)
SG (1) SG11201503980RA (en)
WO (10) WO2014079171A1 (en)

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CN103056152B (en) * 2012-11-23 2016-03-02 华南再生资源(中山)有限公司 biochemical fermentation method and device

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