CN208440534U - Organic refuse treating system - Google Patents
Organic refuse treating system Download PDFInfo
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- CN208440534U CN208440534U CN201820905346.XU CN201820905346U CN208440534U CN 208440534 U CN208440534 U CN 208440534U CN 201820905346 U CN201820905346 U CN 201820905346U CN 208440534 U CN208440534 U CN 208440534U
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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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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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
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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Abstract
The utility model discloses a kind of organic refuse treating systems, including crushing device, anaerobic ferment devices, combustion power generation device, centrifugal dehumidifier, effluent treatment plant, aerobic fermentation device；The crushing device is for being crushed organic waste；The anaerobic ferment devices are used to carry out anaerobic fermentation to broken organic waste, generate biogas and biogas residue；The combustion power generation device is used to carry out combustion power generation using the biogas generated in anaerobic ferment devices；The centrifugal dehumidifier is used to carry out centrifugal dehydration to the biogas residue generated in anaerobic ferment devices, obtains dehydration biogas residue and sewage；The effluent treatment plant is used to carry out purified treatment to the sewage generated in centrifugal dehumidifier, obtains recycle-water；The aerobic fermentation device is used to carry out aerobic fermentation to dehydration biogas residue, forms fertilizer.The organic refuse treating system can sufficiently improve the utilization rate of organic waste, and reduce contamination hazard of the organic waste to environment.
Description
Technical field
The utility model relates to field of garbage disposal, in particular to a kind of organic refuse treating system.
Background technique
Organic garbage of city mainly includes heterogeneous half fluidised form class rubbish (kitchen, fruits and vegetables rubbish) and homogeneous solid-liquid class rubbish
Rubbish (urban night soil, sludge), kitchen garbage therein is mainly derived from the generations such as food processing, food and beverage sevice and resident living
Food residues；Fruits and vegetables rubbish is primarily referred to as the rubbish such as the dish leaf caused by the fields such as agricultural product Transferring Base, the market of farm produce, melon and fruit
Rubbish；Urban night soil and sludge are then respectively from public toilet or residential block septic tank and sewage treatment plant.Due to the organic rubbish in city
The increasingly raising of the continuous variation and environmental quality requirement of rubbish ingredient, conventional process mode such as sanitary landfills, burning and compost
Various drawbacks are gradually shown, have the organic garbage of city anaerobic digestion of efficient waste processing and resource reclaim double effects
Technology obtains pay attention to day by day.
It is quite widely applied currently, being had been obtained using anaerobic digestion techniques processing organic garbage of city in foreign countries,
Just there is large-scale industrial production before the more than ten years.In China, the history of Anaerobic Digestion municipal domestic organic refuse
And it is long-standing, it is mainly used in the processing of feces of livestock and poultry, municipal sludge and high concentrated organic wastewater, most typical application is
The small methane-generating pit in rural area.In recent years, China or is try to utilize in large- and-medium size cities such as Beijing, Shanghai, Guangzhou, Shenzhen
Anaerobic digestion techniques handle the organic garbage of city such as kitchen garbage, municipal sludge.
Although carrying out anaerobic fermentation to organic waste can produce biogas, energy regenerating utilization is carried out, solid matter
Volume reduction rate is not high, if if biogas residue not can be carried out utilization, can also lead to the problem of corresponding post-processing.It can be most using incineration method
The minimizing processing requirement of waste is realized to big degree, but since often moisture content is higher for organic waste, to directly burning band
Come difficult.
Utility model content
The purpose of this utility model is that proposing a kind of organic refuse treating system, organic waste can be sufficiently improved
Utilization rate, and reduce contamination hazard of the organic waste to environment.
In order to achieve the above object, the utility model provides a kind of organic refuse treating system, including crushing device, anaerobism
Installation for fermenting, combustion power generation device, centrifugal dehumidifier, effluent treatment plant, aerobic fermentation device；
The crushing device is for being crushed organic waste；
The anaerobic ferment devices are used to carry out anaerobic fermentation to broken organic waste, generate biogas and biogas residue；
The combustion power generation device is used to carry out combustion power generation using the biogas generated in anaerobic ferment devices；
The centrifugal dehumidifier is used to carry out centrifugal dehydration to the biogas residue generated in anaerobic ferment devices, obtains dehydration natural pond
Slag and sewage；
The effluent treatment plant is used to carry out purified treatment to the sewage generated in centrifugal dehumidifier, is recycled
Water；
The aerobic fermentation device is used to carry out aerobic fermentation to dehydration biogas residue, forms fertilizer.
Optionally, the organic refuse treating system further includes transmission device, the crushing device, anaerobic fermentation dress
Set, centrifugal dehumidifier, aerobic fermentation device are set in the transmitting path of transmission device, and along the sender of transmission device
To being arranged successively.
Optionally, the anaerobic ferment devices include anaeration in normal temperature reactor and high temperature anaerobic reactor, and the medium temperature is detested
At 31 DEG C~34 DEG C, the fermentation temperature of the high temperature anaerobic reactor is controlled 50 DEG C~53 for the fermentation temperature control of oxygen reactor
℃。
Optionally, the anaeration in normal temperature reactor and high temperature anaerobic reactor are set in the transmitting path of transmission device,
And the direction of transfer along transmission device is arranged successively.
Optionally, first gas pipeline, the high temperature are equipped between the anaeration in normal temperature reactor and combustion power generation device
Second gas pipeline is equipped between anaerobic reactor and combustion power generation device.
Optionally, the organic refuse treating system further includes hydrolysis device, and the hydrolysis device is used in organic waste
Gurry be broken device it is broken after and before organic waste enters anaerobic ferment devices, water is carried out to organic waste
Solution.
Optionally, the hydrolysis device is set in the transmitting path of transmission device, and is set to the crushing device and anaerobism
Between installation for fermenting.
Optionally, fluid pipeline, the centrifugal dehydration dress are equipped between the centrifugal dehumidifier and effluent treatment plant
The sewage for setting generation can be entered by fluid pipeline carries out purified treatment in effluent treatment plant.
Optionally, the effluent treatment plant includes membrane bioreactor.
Optionally, the membrane flux of the membrane bioreactor is 12L/ (m2h)-18L/(m2h)。
The utility model has the beneficial effects that the organic refuse treating system of the utility model by organic waste into
Row anaerobic fermentation carries out combustion power generation using the biogas that anaerobic fermentation generates, and it is de- to carry out centrifugation to the biogas residue that anaerobic fermentation generates
Water obtains dehydration biogas residue and sewage, carries out purified treatment to sewage later, obtains recycle-water, and carry out to dehydration biogas residue
Aerobe fermentation obtains fertilizer.The organic refuse treating system of the utility model can sufficiently improve the utilization rate of organic waste,
And reduce contamination hazard of the organic waste to environment.
Detailed description of the invention
It, below will be to attached drawing needed in the embodiment in order to illustrate more clearly of the technical solution of the utility model
It is briefly described, it should be understood that the following drawings illustrates only some embodiments of the utility model, therefore is not construed as
Restriction to scope of protection of the utility model.
Fig. 1 is the structural schematic diagram of the first embodiment of the utility model organic refuse treating system；
Fig. 2 is the structural schematic diagram of the second embodiment of the utility model organic refuse treating system.
Main element symbol description:
10- crushing device；20- anaerobic ferment devices；21- anaeration in normal temperature reactor；22- high temperature anaerobic reactor；30- combustion
Burn power generator；40- centrifugal dehumidifier；50- effluent treatment plant；60- aerobic fermentation device；71- first gas pipeline；
72- second gas pipeline；80- transmission device；90- fluid pipeline；100- hydrolysis device.
Specific embodiment
Below in conjunction with attached drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out clear
Chu is fully described by, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole realities
Apply example.
The component of the utility model embodiment being usually described and illustrated herein in the accompanying drawings can be matched with a variety of different
It sets to arrange and design.Therefore, the detailed description of the embodiments of the present invention provided in the accompanying drawings is not intended to below
The range of claimed invention is limited, but is merely representative of the selected embodiment of the utility model.It is practical based on this
Novel embodiment, those skilled in the art's every other implementation obtained without making creative work
Example, fall within the protection scope of the utility model.
It hereinafter, can the term " includes " used in the various embodiments of the utility model, " having " and its homologous
Word is meant only to indicate special characteristic, number, step, operation, the combination of element, component or aforementioned item, and is understood not to
The combined presence or increasing of one or more other features, number, step, operation, element, component or aforementioned item is excluded first
A possibility that adding the combination of one or more features, number, step, operation, element, component or aforementioned item.
In the various embodiments of the utility model, statement " A or/and B " includes any combination of the text listed file names with
Or all combinations, it may include A, may include B or may include A and B both.
In the description of the present invention, it should be understood that term " longitudinal direction ", " transverse direction ", "upper", "lower", " preceding ",
The orientation or positional relationship of the instructions such as " rear ", "left", "right", "vertical", " transverse direction ", "top", "bottom", "inner", "outside" be based on
Orientation or positional relationship shown in the drawings, is merely for convenience of describing the present invention and simplifying the description, rather than instruction or dark
Show that signified device or element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as pair
The limitation of the utility model.In addition, term " first ", " second ", " third " etc. are only used for distinguishing description, and should not be understood as referring to
Show or imply relative importance.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " example ", " specifically show
The description of example " or " some examples " etc. means specific features, structure, material or spy described in conjunction with this embodiment or example
Point is contained at least one embodiment or example of the utility model.In the present specification, to the schematic table of above-mentioned term
Stating may not refer to the same embodiment or example.Moreover, particular features, structures, materials, or characteristics described can be
It can be combined in any suitable manner in any one or more embodiment or examples.
In the description of the present invention, unless otherwise specified and limited, it should be noted that term " installation ", " phase
Even ", " connection " shall be understood in a broad sense, for example, it may be mechanical connection, the connection being also possible to inside two elements can be
It is connected directly, can also indirectly connected through an intermediary, for the ordinary skill in the art, it can be according to specific
Situation understands the concrete meaning of above-mentioned term.Unless otherwise defined, otherwise all terms used herein (including technical term
With scientific term) with identical as the various normally understood meanings of embodiment one skilled in the art of the utility model
Meaning.The term (term such as limited in the dictionary generally used) is to be interpreted as having and lead in the relevant technologies
The identical meaning of situational meaning in domain and it will be interpreted as having Utopian meaning or meaning too formal, unless
It is clearly defined in the various embodiments of the utility model.
Please refer to Fig. 1 and Fig. 2, the utility model provides a kind of organic refuse treating system, including crushing device 10, detests
Aerobe fermentation device 20, combustion power generation device 30, centrifugal dehumidifier 40, effluent treatment plant 50, aerobic fermentation device 60；
The crushing device 10 is for being crushed organic waste；
The anaerobic ferment devices 20 are used to carry out anaerobic fermentation to broken organic waste, generate biogas and natural pond
Slag；
The combustion power generation device 30 is used to carry out combustion power generation using the biogas generated in anaerobic ferment devices 20；
The centrifugal dehumidifier 40 is used to carry out centrifugal dehydration to the biogas residue generated in anaerobic ferment devices 20, is taken off
Water biogas residue and sewage；
The effluent treatment plant 50 is used to carry out purified treatment to the sewage generated in centrifugal dehumidifier 40, is returned
Receive water；
The aerobic fermentation device 60 is used to carry out aerobic fermentation to dehydration biogas residue, forms fertilizer.
Optionally, the organic refuse treating system further includes transmission device 80, the crushing device 10, anaerobic fermentation
Device 20, centrifugal dehumidifier 40, aerobic fermentation device 60 fill in the transmitting path of transmission device 80 along transmission
80 direction of transfer is set to be arranged successively.
Optionally, the organic waste includes garbage, kitchen garbage, municipal sludge, market of farm produce rubbish and fowl
The combination of animal manure one or more of just.
Specifically, organic waste can be crushed to 10mm hereinafter, organic to be obviously improved by the crushing device 10
The anaerobic fermentation efficiency of waste.
Specifically, during the anaerobic ferment devices 20 carry out Anaerobic Treatment to organic waste, organic waste
Biogas is released by microorganism decomposition in the state of lacking oxygen.
Optionally, as shown in Figures 1 and 2, the anaerobic ferment devices 20 include that anaeration in normal temperature reactor 21 is detested with high temperature
Oxygen reactor 22, the fermentation temperature control of the anaeration in normal temperature reactor 21 is at 31 DEG C~34 DEG C, the high temperature anaerobic reactor
22 fermentation temperature is controlled at 50 DEG C~53 DEG C.
The anaeration in normal temperature reactor 21 is set in the transmitting path of transmission device 80 with high temperature anaerobic reactor 22, and
And it is arranged successively along the direction of transfer of transmission device 80.
First gas pipeline 71 is equipped between the anaeration in normal temperature reactor 21 and combustion power generation device 30, the high temperature is detested
Second gas pipeline 72 is equipped between oxygen reactor 22 and combustion power generation device 30.
The anaeration in normal temperature reactor 21 carries out fermentation process, the anaeration in normal temperature reactor 21 to organic waste first
The biogas of middle generation is entered in combustion power generation device 30 by first gas pipeline 71 carries out combustion power generation, and the anaeration in normal temperature is anti-
The biogas residue generated in device 21 is answered to continue to ferment into high temperature anaerobic reactor 22 by transmission device 80；
The biogas generated in the high temperature anaerobic reactor 22 enters combustion power generation device 30 by second gas pipeline 72
Middle carry out combustion power generation, the biogas residue generated in the high temperature anaerobic reactor 22 enter centrifugal dehumidifier by transmission device 80
It is carried out dehydrating in 40.
The utility model utilize in the anaerobic fermentation method that combines of mild high-temperature-phase, using anaeration in normal temperature reactor 21 to having
Machine waste enters back into after being pre-processed carries out hot fermentation in high temperature anaerobic reactor 22, can be realized system stable operation
And obtain higher production rate of methane.
Optionally, as shown in Fig. 2, the organic refuse treating system further includes hydrolysis device 100, the hydrolysis device
100 for organic waste be broken device 10 it is broken after and organic waste enter anaerobic ferment devices 20 it
Before, organic waste is hydrolyzed, the efficiency of anaerobic fermentation is able to ascend, is needed in hydrolytic process to broken organic waste
Hydrolase is added in gurry, the hydrolase includes cellulase, hemicellulase.
Specifically, the hydrolysis device 100 is set in the transmitting path of transmission device 80, and it is set to the crushing device 10
Between anaerobic ferment devices 20.
Specifically, being equipped with fluid pipeline 90, the centrifugation between the centrifugal dehumidifier 40 and effluent treatment plant 50
The sewage generated in dehydration device 40 can be entered in effluent treatment plant 50 by fluid pipeline 90 carries out purified treatment.
Specifically, the dehydration biogas residue that biogas residue after the centrifugal dehumidifier 40 is carried out dehydrating, obtains is aqueous
Amount is less than 70wt%, since the water content of dehydration biogas residue is lower, mature speed when using its progress aerobic fermentation production fertilizer
Degree is very fast, compared with the biogas residue not being dehydrated, is dehydrated 50% or more the improved efficiency of biogas residue fermenting-ripening.
Specifically, the effluent treatment plant 50 includes membrane bioreactor (Membrane Bio-Reactor, MBR).
Optionally, the membrane flux of the membrane bioreactor is 12L/ (m2h) -18L/ (m2h).
Membrane bioreactor is a kind of novel state wastewater treatment system combined by film separation unit with biological processing unit
System.Replace the secondary settling tank of traditional biological processing technique end with membrane module, keep high activity sludge concentration in the bioreactor,
Biological treatment organic loading is improved, to reduce sewage treatment facility occupied area, and surplus by keeping low sludge loading to reduce
Remaining sludge quantity.It mainly utilizes activated sludge and larger molecular organics in membrane separation plant trap water.Membrane bioreactor because
Its effective crown_interception can retain generation cycle longer microorganism, it can be achieved that Simultaneous Nitrification bacterium exists to deep purification of waste water
It can sufficiently be bred in system, nitrification effect is obvious, and providing deep phosphorous removal denitrogenation may.
Membrane bioreaction technology has not only effectively achieved the purpose of mud-water separation, but also has tertiary sewage treatment tradition
The incomparable advantage of technique:
1, it is efficiently separated by solid-liquid separation, separating effect is much better than traditional sedimentation basin, and effluent quality is good, and water outlet is outstanding
Floating object and turbidity close to zero, can direct reuse, realize sewage recycling；
2, the efficient crown_interception of film, is completely trapped at microorganism in bioreactor, realizes reactor hydraulic retention
Time (HRT) and sludge age (SRT's) is kept completely separate, and operation control is flexibly stablized；
3, the aeration tank that traditional wastewater is handled and secondary settling tank are combined into one due to MBR, and instead of the complete of tertiary treatment
Portion's process facility, therefore occupied area can be greatly decreased, save construction investment；
4, conducive to the retention of nitrobacteria and breeding, system nitrification efficiency is high.Can also have by the change of the method for operation de-
Ammonia and phosphorus removal functional；
5, since sludge age can be grown very much, to greatly improve the degradation efficiency of hardly degraded organic substance；
6, reactor is run under high volumetric loading, low sludge loading, long sludge age, and excess sludge production is extremely low, due to mud
Age can endless, can theoretically realize zero sludge discharge；
7, system realizes PLC control, convenient operation and management.
Specifically, after effluent treatment plant 50, sewage becomes clean recycle-water, the recycle-water can connect to
Anaerobic ferment devices 20 realize the charge dilution of organic waste, can also pour to flowers, plants and trees, be also used as ring
The clean water in border.
The biogas residue generated through anaerobic fermentation contains a large amount of undegradable organic matters, therefore carries out aerobic fermentation heap using biogas residue
Fertilizer can be realized the minimizing of rubbish, recycling and innoxious.
The organic refuse treating system of the utility model is sent out by carrying out anaerobic fermentation to organic waste using anaerobism
The biogas that ferment generates carries out combustion power generation, carries out centrifugal dehydration to the biogas residue that anaerobic fermentation generates, obtains dehydration biogas residue and sewage,
Purified treatment is carried out to sewage later, recycle-water is obtained, and aerobic fermentation is carried out to dehydration biogas residue, obtains fertilizer.This is practical
Novel organic refuse treating system can sufficiently improve the utilization rate of organic waste, and reduce organic waste to environment
Contamination hazard.
It is further described below with reference to organic refuse treating system of 2 specific embodiments to the utility model.
Embodiment 1
Fig. 1 is the structural schematic diagram of the first embodiment of the utility model organic refuse treating system, as shown in Figure 1,
The first embodiment provides a kind of organic refuse treating system, including the reaction of transmission device 80, crushing device 10, anaeration in normal temperature
Device 21, high temperature anaerobic reactor 22, combustion power generation device 30, centrifugal dehumidifier 40, effluent treatment plant 50, aerobic fermentation dress
Set 60；
It is the crushing device 10, anaeration in normal temperature reactor 21, high temperature anaerobic reactor 22, centrifugal dehumidifier 40, aerobic
Installation for fermenting 60 is arranged successively in the transmitting path of transmission device 80 along the direction of transfer of transmission device 80；
Fluid pipeline 90 is equipped between the centrifugal dehumidifier 40 and effluent treatment plant 50；
First gas pipeline 71 is equipped between the anaeration in normal temperature reactor 21 and combustion power generation device 30, the high temperature is detested
Second gas pipeline 72 is equipped between oxygen reactor 22 and combustion power generation device 30.
Embodiment 2
Fig. 2 is the structural schematic diagram of the second embodiment of the utility model organic refuse treating system, as shown in Fig. 2,
The second embodiment provides a kind of organic refuse treating system, including transmission device 80, crushing device 10, hydrolysis device 100,
Anaeration in normal temperature reactor 21, high temperature anaerobic reactor 22, combustion power generation device 30, centrifugal dehumidifier 40, effluent treatment plant
50, aerobic fermentation device 60；
The crushing device 10, hydrolysis device 100, anaeration in normal temperature reactor 21, high temperature anaerobic reactor 22, centrifugal dehydration
Device 40, aerobic fermentation device 60 are set in the transmitting path of transmission device 80, and along the direction of transfer of transmission device 80
It is arranged successively；
Fluid pipeline 90 is equipped between the centrifugal dehumidifier 40 and effluent treatment plant 50；
First gas pipeline 71 is equipped between the anaeration in normal temperature reactor 21 and combustion power generation device 30, the high temperature is detested
Second gas pipeline 72 is equipped between oxygen reactor 22 and combustion power generation device 30.
Disclosed above is only the specific implementation scene of the utility model, but the protection scope of the utility model is not limited to
In this, anyone skilled in the art within the technical scope disclosed by the utility model, can readily occur in variation
Or replacement, it should be covered within the scope of the utility model.
Claims (10)
1. a kind of organic refuse treating system, which is characterized in that including crushing device, anaerobic ferment devices, combustion power generation dress
It sets, centrifugal dehumidifier, effluent treatment plant, aerobic fermentation device；
The crushing device is for being crushed organic waste；
The anaerobic ferment devices are used to carry out anaerobic fermentation to broken organic waste, generate biogas and biogas residue；
The combustion power generation device is used to carry out combustion power generation using the biogas generated in anaerobic ferment devices；
The centrifugal dehumidifier is used to carry out centrifugal dehydration to the biogas residue that generates in anaerobic ferment devices, obtain dehydration biogas residue with
Sewage；
The effluent treatment plant is used to carry out purified treatment to the sewage generated in centrifugal dehumidifier, obtains recycle-water；
The aerobic fermentation device is used to carry out aerobic fermentation to dehydration biogas residue, forms fertilizer.
2. organic refuse treating system according to claim 1, which is characterized in that it further include transmission device, it is described broken
Crushing device, anaerobic ferment devices, centrifugal dehumidifier, aerobic fermentation device are set in the transmitting path of transmission device, and
Direction of transfer along transmission device is arranged successively.
3. organic refuse treating system according to claim 2, which is characterized in that during the anaerobic ferment devices include
Warm anaerobic reactor and high temperature anaerobic reactor, the fermentation temperature control of the anaeration in normal temperature reactor is at 31 DEG C~34 DEG C, institute
The fermentation temperature for stating high temperature anaerobic reactor is controlled at 50 DEG C~53 DEG C.
4. organic refuse treating system according to claim 3, which is characterized in that the anaeration in normal temperature reactor and height
Warm anaerobic reactor is set in the transmitting path of transmission device, and is arranged successively along the direction of transfer of transmission device.
5. organic refuse treating system according to claim 3, which is characterized in that the anaeration in normal temperature reactor and combustion
It burns and is equipped with first gas pipeline between power generator, the second gas is equipped between the high temperature anaerobic reactor and combustion power generation device
Body pipeline.
6. organic refuse treating system according to claim 2, which is characterized in that it further include hydrolysis device, the water
Solution device be used for organic waste be broken device it is broken after and before organic waste enters anaerobic ferment devices,
Organic waste is hydrolyzed.
7. organic refuse treating system according to claim 6, which is characterized in that the hydrolysis device is set to transmission dress
In the transmitting path set, and it is set between the crushing device and anaerobic ferment devices.
8. organic refuse treating system according to claim 1, which is characterized in that the centrifugal dehumidifier and sewage
Fluid pipeline is equipped between purification device, the sewage generated in the centrifugal dehumidifier can enter sewage by fluid pipeline
Purified treatment is carried out in purification device.
9. organic refuse treating system according to claim 1, which is characterized in that the effluent treatment plant includes film
Bioreactor.
10. organic refuse treating system according to claim 9, which is characterized in that the film of the membrane bioreactor
Flux is 12L/ (m2h)-18L/(m2h)。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820905346.XU CN208440534U (en) | 2018-06-11 | 2018-06-11 | Organic refuse treating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820905346.XU CN208440534U (en) | 2018-06-11 | 2018-06-11 | Organic refuse treating system |
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| Publication Number | Publication Date |
|---|---|
| CN208440534U true CN208440534U (en) | 2019-01-29 |
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ID=65089938
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| CN201820905346.XU Active CN208440534U (en) | 2018-06-11 | 2018-06-11 | Organic refuse treating system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020220411A1 (en) * | 2019-04-30 | 2020-11-05 | 贵州民族大学 | Integrated treatment system for rural domestic garbage |
| CN115069743A (en) * | 2022-06-20 | 2022-09-20 | 四川逸名环保科技有限公司 | Sewage and garbage global treatment recycling method, device and control method |
-
2018
- 2018-06-11 CN CN201820905346.XU patent/CN208440534U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020220411A1 (en) * | 2019-04-30 | 2020-11-05 | 贵州民族大学 | Integrated treatment system for rural domestic garbage |
| CN115069743A (en) * | 2022-06-20 | 2022-09-20 | 四川逸名环保科技有限公司 | Sewage and garbage global treatment recycling method, device and control method |
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