CN105478443A - In-situ reduction type integrated device and treatment method for household garbage - Google Patents
In-situ reduction type integrated device and treatment method for household garbage Download PDFInfo
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- CN105478443A CN105478443A CN201510977639.XA CN201510977639A CN105478443A CN 105478443 A CN105478443 A CN 105478443A CN 201510977639 A CN201510977639 A CN 201510977639A CN 105478443 A CN105478443 A CN 105478443A
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- 238000000034 method Methods 0.000 title claims abstract description 17
- 238000011065 in-situ storage Methods 0.000 title abstract description 3
- 239000000463 material Substances 0.000 claims abstract description 49
- 238000006243 chemical reaction Methods 0.000 claims abstract description 39
- 238000003756 stirring Methods 0.000 claims abstract description 31
- 239000010802 sludge Substances 0.000 claims description 19
- 238000000855 fermentation Methods 0.000 claims description 16
- 230000004151 fermentation Effects 0.000 claims description 15
- 238000007599 discharging Methods 0.000 claims description 12
- 239000002245 particle Substances 0.000 claims description 10
- 239000012535 impurity Substances 0.000 claims description 9
- 238000013467 fragmentation Methods 0.000 claims description 8
- 238000006062 fragmentation reaction Methods 0.000 claims description 8
- 238000012216 screening Methods 0.000 claims description 7
- 238000005273 aeration Methods 0.000 claims description 4
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims description 4
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- 230000009286 beneficial effect Effects 0.000 description 1
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C4/00—Crushing or disintegrating by roller mills
- B02C4/02—Crushing or disintegrating by roller mills with two or more rollers
- B02C4/08—Crushing or disintegrating by roller mills with two or more rollers with co-operating corrugated or toothed crushing-rollers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C4/00—Crushing or disintegrating by roller mills
- B02C4/28—Details
- B02C4/30—Shape or construction of rollers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention discloses an in-situ reduction type integrated device and treatment method for household garbage. A lifting device is arranged on one side of a device body and is used for lifting the garbage and pouring the garbage into a crushing device located on the top of the device body; an outlet of the crushing device is connected to a feed port of an aerobic reaction twin-cylinder body through a conveying device; the aerobic reaction twin-cylinder body is composed of two aerobic reactors serially connected, a stirring rotor used for pushing and stirring material is arranged in each aerobic reactor along the axis, and one ends of the stirring rotors are connected to a driving device driving the stirring rotors to rotate; a vibrating screen is arranged below a discharge port of the aerobic reaction twin-cylinder body. According to the invention, the integrated crushing and reducing treatment is adopted for rural garbage and is suitable for mixed or classified garbage of various kinds; the cascading type stirring and conveying mode is adopted, material is separately fermented at different stages, and the putrescibility of the material is improved; the device is compact in overall structure, small in occupied area, convenient to disassemble and assemble and easy to maintain.
Description
Technical field
The invention belongs to field of garbage disposal, especially relate to one way of life rubbish sludge reduction onsite integrated apparatus and processing method thereof.
Background technology
China's people in the countryside account for the 60%-70% of country's total population, along with the fast development of China's villages and small towns economy, villages and small towns resident living mode and production model develop, and villages and small towns Output of Domestic Waste increases day by day, according to statistics, national villages and small towns produce house refuse about 1.64 hundred million tons every year.China rural garbage has a polydispersion, distributes wide, collects transhipment difficulty; Nitrogen, phosphorus and the content of organic matter are high, easy pollution of ecological environment; The features such as geographic difference is remarkable, and seasonal variety is comparatively large, difficult.Because of heap garbage the like waste, the occupied farmland area with damaging is more than 2,000,000 mu in the whole nation, and the investigation that Tenth Five-Year Plan Period is done in Taihu Lake region shows, the rubbish degree of depth accumulated in river course is all in the scope of 1-2m.Rubbish disorderly falls, arbitrarily stacks, severe contamination water body and soil environment, directly affect rural potable water and agricultural product security, causes human settlement to be worsened, ecological environment and agricultural sustainable development are constituted a serious threat, the process of restriction rural area well-off society of China and new countryside construction.In process disposal, China rural garbage is burned with simple and easy landfill, outdoor or local method, simple stack retting and traditional anaerobic fermentation be for main processing ways.The quick growth of rural garbage is build the bottleneck factor of " cleanliness of villages " new socialist countryside with the serious backwardness of process disposal technology.The rural garbage problem solved is the preferential content of " 12 " National Program for Medium-to Long-term Scientific and Technological Development, planning lists " comprehensive anti-pollution and recycling waste ", " widespread pollution from the overuse of fertilizers and pesticides in rural area controls " in environmental area preferential theme, propose emphasis research and development rural garbage high efficient resourcing comprehensive utilization key technology and equipment, build rural garbage and recycle and overall process EMS.Pushing forward the building of a new socialist countryside is the vital task of China " 12 " period, and ensureing rural environment safety, improving the level of resource utilization of rural development is one, new socialist countryside important content.At present, some are have developed efficiently based on the rural garbage minimizing resource technology of rural garbage classification, but the effect of real rural garbage classification is not fully up to expectations, containing a large amount of plastics, glass, pop can, textile, metal impurities, often there is the problems such as heavy substance is serious for equipment attrition, polybag wrapping phenomena serious, living beings separative efficiency is lower, fertilizer efficiency is poor in sludge reduction onsite process, has a strong impact on follow-up agricultural.Therefore, a set of residents in rural community sludge reduction onsite integrated apparatus and processing method thereof are developed in active demand, effectively solve a villages and small towns house refuse highly effective and safe application technology as the second resource difficult problem.
Summary of the invention
In order to overcome the defect of technology or equipment in background technology, the object of the present invention is to provide one way of life rubbish sludge reduction onsite integrated apparatus and processing method thereof, realizing residents in rural community original position significantly decrement, obtaining the living beings of high rotten degree; Avoid heavy substance in material to the wearing and tearing of equipment, to solve a difficult problem for plastic winding main shaft simultaneously.
To achieve these goals, the technical solution used in the present invention is as follows:
One way of life rubbish sludge reduction onsite integrated apparatus, comprising: device body side is provided with lifting device, for promoting rubbish and pouring the breaker being positioned at device body top into; Breaker outlet is connected by conveying device with between the charging aperture of aerobic reaction double shell; Described aerobic reaction double shell is made up of the aerobic reactor of two series connection, and be all provided with one in each aerobic reactor along axle center for pushing and stirring the stirring rotator of material, stirring rotator one end is connected with the drive unit driving its rotation; The discharging opening of aerobic reaction double shell divides into vibratory sieve.
As preferably, described stirring rotator is made up of central shaft, conveyor screw and stirrer paddle, and conveyor screw is fixed on this central shaft side with one heart and is tapering type extension from axle head to axle centre position, for axially pushing material; Stirrer paddle and conveyor screw are coaxially fixed on this central shaft opposite side; The laying standard of some stirrer paddles is: the propelling movement power not producing centrally axle axis in rotary course.
As preferably, described described stirrer paddle cross section assumes diamond in shape, and rhombus major axis is axially parallel with central shaft; Stirrer paddle is laid on different equidistant sagittal plane of central shaft, and the paddle type that the stirrer paddle in each plane is formed is straight leaf open turbine formula; Stirrer paddle quantity on different sagittal plane equal and centrally the projection of axle axis direction overlap.
As preferred further, described aerobic reaction double shell is made up of the first aerobic reaction cylindrical shell and the second aerobic reacting cylinder body; Described charging aperture is arranged at the one end near conveyor screw on the first aerobic reaction cylindrical shell, described discharging opening is arranged at the one end near stirrer paddle in the second aerobic reacting cylinder body, and the first aerobic reaction cylindrical shell is connected by cylindrical shell connector with the one end near conveyor screw in the second aerobic reacting cylinder body near one end of stirrer paddle.
As preferably, between the first described aerobic reaction cylindrical shell and the second aerobic reacting cylinder body, there is difference in height, make the angle of inclination between cylindrical shell connector and horizontal plane be 40 ° ~ 60 °.
As preferably, described breaker adopts double-roll crusher, and double-roll crusher comprises crushing teeth, broken chamber, travelling gear; A pair crushing toothed roller be arranged crosswise in broken chamber, and to be axially connected with travelling gear respectively, to be rotated by the synchronized reverse drive of travelling gear, the uniform crushing teeth of axis on crushing toothed roller.
As preferred further, described crushing teeth is arc inner tooth, axially uniform 8 ~ 14; Described described vibratory sieve comprises flat-surfaced screen, screening bin, support pedestal, vibrating motor; Flat-surfaced screen is in tilted layout in screening bin, and angle of inclination is 5 ° ~ 6.3 °; Vibrating motor is placed on the downside of flat-surfaced screen, 1/3rd places from the front end.
As preferably, described described conveying device adopts ribbon conveyer, the threephase asynchronous machine that described drive unit comprises reductor and matches, and described lifting device is lift rail.
Utilize a house refuse sludge reduction onsite integral treatment method for described device, comprise the steps:
Tubbiness rubbish is promoted by dustbin lifting device, and tilt to pour breaker into and carry out broken bag break process, the rubbish after fragmentation falls to band conveying device; By conveying device the rubbish after fragmentation is delivered to the first aerobic reaction cylindrical shell and the second aerobic reacting cylinder body is fermented, in the first aerobic reaction cylindrical shell and the second aerobic reacting cylinder body at control temperature 60 ~ 70 DEG C, utilize the yeasting that blast aeration remains aerobic, stirred by the conveying of stirring rotator, material is carried out layer-transferred fermentation and reduces living beings particle diameter, other impurity keeps particle diameter at 3 ~ 7cm; Material after fermentation is delivered in vibratory sieve through discharging opening, carries out that material is homogeneous, removal of impurities through vibratory sieve continuous shaking.
Compared with background technology, the beneficial effect that the present invention has is:
The present invention adopts rural garbage Integral-crushing decrement treatment, is applicable to mixing and sorted various garbage, solves the problem of plastic winding main shaft, improves stable equipment operation.
The present invention can realize original position significantly decrement to residents in rural community, significantly promotes living beings purity, can direct agricultural reutilization.
The present invention adopts layer-transferred to stir conveying, and the split of Different periods material is fermented, and improves material rotten degree.
Single unit system compact conformation of the present invention, floor space is little, easy accessibility, is easy to safeguard.
Accompanying drawing explanation
Fig. 1 is the overall structure schematic diagram of one way of life rubbish sludge reduction onsite integrated apparatus;
Fig. 2 is double-roll crusher schematic diagram of the present invention;
Fig. 3 is crushing teeth schematic diagram of the present invention;
Fig. 4 is aerobic reaction double shell schematic diagram of the present invention;
Fig. 5 is vibratory sieve schematic diagram of the present invention;
Fig. 6 is stirring rotator schematic diagram of the present invention.
In figure: 1, lifting device, 2, breaker, 3, conveying device, 4, aerobic reaction double shell, 5, reductor, 6, threephase asynchronous machine, 7, vibratory sieve, 8, stirring rotator, 2-1, broken chamber, 2-2, travelling gear, 2-3, crushing teeth, 4-1, charging aperture, 4-2, first aerobic reaction cylindrical shell, 4-3, cylindrical shell connector, 4-4, second aerobic reacting cylinder body, 4-5, discharging opening, 7-1, flat-surfaced screen, 7-2, screening chamber, 7-3, support pedestal, 7-4, vibrating motor, 8-1, central shaft, 8-2, tapering type spiral, 8-3, rhombus blade.
Detailed description of the invention
Below in conjunction with drawings and Examples, the invention will be further described.
As shown in Figure 1 and Figure 2, one way of life rubbish sludge reduction onsite integrated apparatus, comprising: device body side is provided with lifting device 1, for promoting rubbish and pouring the breaker 2 being positioned at device body top into; Breaker 2 is exported and is connected by conveying device 3 between the charging aperture 4-1 of aerobic reaction double shell 4; Described aerobic reaction double shell 4 is made up of the aerobic reactor of two series connection, and be all provided with one in each aerobic reactor along axle center for pushing and stirring the stirring rotator 8 of material, stirring rotator 8 one end is connected with the drive unit 10 driving its rotation; The discharging opening 4-5 of aerobic reaction double shell 4 divides into vibratory sieve 7.
Operation principle of the present invention and process as follows:
The tubbiness rubbish collected is promoted by dustbin lifting device 1, tilt to pour breaker 2 into and carry out broken bag break process, breaker 2 is by its shear action, and by composting or sorted refuse breaking to particle diameter 3 ~ 7cm, the rubbish after fragmentation falls in conveying device 3; Rubbish after fragmentation is delivered to charging aperture 4-1 by conveying device 3, aerobic reaction double shell 4 carries out associating stepwise fermentation, by at the layer-transferred conveying stirring of stirring rotator 8 and control temperature 60 ~ 70 DEG C in cylindrical shell, by material fermentation, fermentation aerobic environment is realized by blast aeration, living beings particle diameter is fermented dehydration gradually, and particle diameter reduces.Other impurity cannot ferment, and keep original particle diameter 3 ~ 7cm; Material after fermentation in vibratory sieve 7, to realize that living beings are homogeneous, removal of impurities through discharging opening 4-5 by material difference through vibratory sieve continuous shaking.Obtain purity be greater than 95% living beings of becoming thoroughly decomposed can direct utilization.Agitating device is fixed in reactor, is pushed by the material entering reactor by conveyor screw along convergent direction, arrives stirrer paddle region.Stirrer paddle, by stirring material, makes it fully mix and ferment.The material fermented the most at last exports to outside reactor, realizes processing continuously.
As shown in Figure 6, stirring rotator 8 is made up of central shaft 8-1, conveyor screw 8-2 and stirrer paddle 8-3, and conveyor screw 8-2 is fixed on this central shaft 8-1 side with one heart and is tapering type extension from axle head to axle centre position, for axially pushing material; Stirrer paddle 9 and conveyor screw 7 are coaxially fixed on this central shaft 8-1 opposite side; The laying standard of some stirrer paddles 9 is: the propelling movement power not producing centrally axle 8-1 axis in rotary course.
And the reason arranging this laying standard is: in fill process, if stopping charging, then conveyor screw can not produce propelling movement power to the bank body in reactor, and the pushed circumferential stirring only receiving stirrer paddle to stirrer paddle, but can not pushed outwardsly further give.Therefore, the same batch of material entered all can concentrate in a certain FX, and can not with the mixing of materials of other batches.Current one batch of material entered is fermented to time to a certain degree, can add materials in conveyor screw further, utilizes new material outwards to be pushed by fermented-material, forms layering fermentation system in reactor.This system can reduce the composite rate of new marine store greatly, effectively controls the solid material time of staying in the reactor, improves the degradation efficiency of outputting material, promotes end product quality.
In present embodiment, and increase the raising blade stirring rigidity of stirrer paddle, improve anti-interference intensity and toughness, stirrer paddle 9 cross section assumes diamond in shape, and rhombus major axis is axially parallel with central shaft 8-1.During stirring, stirrer paddle contacts material with largest face, fully stirs the material of blade periphery, makes it ferment evenly.
Stirrer paddle 9 is laid on different equidistant sagittal plane of central shaft 8-1, and the paddle type that the stirrer paddle 9 in each plane is formed is straight leaf open turbine formula.The blade of this formal distribution makes filler radially flow, and has axial stream hardly, the axial backmixing decreasing new and old storeroom of therefore trying one's best.Stirrer paddle 9 quantity on different sagittal plane equal and centrally the projection of axle 8-1 axis direction overlap.The attitude be arranged on central shaft of the stirrer paddle namely on different sagittal plane is identical, not dislocation between blade.The blade that there is dislocation also can cause material to be advanced by discrete great-jump-forward, increases the axial backmixing rate of material.Equidistant sagittal plane can make material can with metastable speed charging, and the reaction of each section is comparatively even, is convenient to control.
The core difficult problem that solid waste in-situ fermentation exists is that residence time of material is long, material becomes thoroughly decomposed uneven, the main cause causing this problem to produce is that the mixing of materials of the different time of staying is excessive, particularly in dynamic response device, when there is biological respinse, between material, axial backmixing rate is higher, causes the time of staying that accurately cannot control material.At present, on market existing twin axle structure of reactor and the present invention similar, but inside reactor arranges two shafts side by side.In order to form contrast, by single axle reactor of the present invention and twin axle reactor, by using the modeling of EDEM discrete element, calculating simulation is carried out to its axial backmixing rate.Found by simulation, twin axle reactor is while realizing material laminar flow, and axial backmixing rate reaches more than 42%; And single axle reactor is found by simulation, axial backmixing rate is only 17%, is obviously better than twin axle reactor.In effective realization response device, the layer-transferred fermentation of material is particularly applicable to layering fermentation, and Different periods mixing of materials ratio is little, ensures that the same period fully mixes simultaneously, fully contact with medium, microorganism, the time of staying of accurate control each section of material, improve Fermentation efficiency, ensure product quality.Compared to twin axle reactor, it is more than the twice of twin axle reactor that single axle reactor obtains product rotten degree (percentage of seedgermination), can reach more than 50%.
As shown in Figure 4, aerobic reaction double shell 4 is made up of the first aerobic reaction cylindrical shell 4-2 and the second aerobic reacting cylinder body 4-5; Described charging aperture 4-1 is arranged at the one end near conveyor screw 8-2 on the first aerobic reaction cylindrical shell 4-2, described discharging opening 4-5 is arranged at the one end near stirrer paddle 8-3 on the second aerobic reacting cylinder body 4-5, and the first aerobic reaction cylindrical shell 4-2 is connected by cylindrical shell connector 4-3 with the one end near conveyor screw 8-2 on the second aerobic reacting cylinder body 4-5 near one end of stirrer paddle 8-3.In cylindrical shell, material is delivered to discharging opening 4-5 by charging aperture 4-1 through cylindrical shell connector 4-3 by two stirring rotators 8.The peripheral uniform pivot flange of aerobic reaction double shell 4.
Between first aerobic reaction cylindrical shell 4-2 and the second aerobic reacting cylinder body 4-5, there is difference in height, make the angle of inclination between cylindrical shell connector 4-3 and horizontal plane be 40 ° ~ 60 °.
As shown in Figure 2, breaker 2 adopts double-roll crusher, and double-roll crusher comprises crushing teeth 2-3, broken chamber 2-1, travelling gear 2-2; A pair crushing toothed roller be arranged crosswise in broken chamber 2-1, and to be axially connected with travelling gear 2-2 respectively, to be rotated by the synchronized reverse drive of travelling gear, the uniform crushing teeth 2-3 of axis on crushing toothed roller.
As shown in Figure 3, described crushing teeth 2-3 is arc inner tooth, axially uniform 8 ~ 14.As shown in Figure 5, described described vibratory sieve 7 comprises flat-surfaced screen 7-1, screening bin 7-2, support pedestal 7-3, vibrating motor 7-4; Flat-surfaced screen 7-1 is in tilted layout in screening bin 7-2, and angle of inclination is 5 ° ~ 6.3 °; Vibrating motor 7-4 is placed on the downside of flat-surfaced screen 7-1,1/3rd places from the front end.
In present embodiment, conveying device 3 adopts ribbon conveyer, the threephase asynchronous machine 6 that described drive unit 10 comprises reductor 5 and matches, and described lifting device 1 is lift rail.
Based on the one way of life rubbish sludge reduction onsite integral treatment method that said apparatus carries out, comprise the steps:
Tubbiness rubbish is promoted by dustbin lifting device 1, tilts to pour breaker 2 into and carries out broken bag break process, and the rubbish after fragmentation falls to band conveying device 3; By conveying device 3 rubbish after fragmentation is delivered to the first aerobic reaction cylindrical shell 4-2 and the second aerobic reacting cylinder body 4-5 ferments, in the first aerobic reaction cylindrical shell 4-2 and the second aerobic reacting cylinder body 4-5 at control temperature 60 ~ 70 DEG C, utilize the yeasting that blast aeration remains aerobic, stirred by the conveying of stirring rotator 8, material is carried out layer-transferred fermentation and reduces living beings particle diameter, other impurity keeps particle diameter at 3 ~ 5cm; Material after fermentation is delivered in vibratory sieve 7 through discharging opening 4-5, carries out that material is homogeneous, removal of impurities through vibratory sieve continuous shaking.
As can be seen here, present invention achieves residents in rural community original position significantly decrement, be applicable to multiple character waste reduction.Effective solution plastic winding problem, refuse decomposing degree is high; Compact conformation, easy accessibility, be easy to safeguard, obvious technical effects is given prominence to.
Claims (9)
1. one way of life rubbish sludge reduction onsite integrated apparatus, is characterized in that, comprising: device body side is provided with lifting device (1), for promoting rubbish and pouring the breaker (2) being positioned at device body top into; Be connected by conveying device (3) between breaker (2) outlet and the charging aperture (4-1) of aerobic reaction double shell (4); Described aerobic reaction double shell (4) is made up of the aerobic reactor of two series connection, all be provided with one in each aerobic reactor along axle center for pushing and stirring the stirring rotator (8) of material, stirring rotator (8) one end is connected with the drive unit (10) driving its rotation; The discharging opening (4-5) of aerobic reaction double shell (4) divides into vibratory sieve (7).
2. house refuse sludge reduction onsite integrated apparatus as claimed in claim 1, it is characterized in that: described stirring rotator (8) is made up of central shaft (8-1), conveyor screw (8-2) and stirrer paddle (8-3), conveyor screw (8-2) is fixed on this central shaft (8-1) side with one heart and is tapering type extension from axle head to axle centre position, for axially pushing material; Stirrer paddle (9) and conveyor screw (7) are coaxially fixed on this central shaft (8-1) opposite side; The laying standard of some stirrer paddles (9) is: in rotary course, do not produce the propelling movement power that centrally axle (8-1) is axial.
3. house refuse sludge reduction onsite integrated apparatus as claimed in claim 1, is characterized in that: described described stirrer paddle (9) cross section assumes diamond in shape, and rhombus major axis is axially parallel with central shaft (8-1); Stirrer paddle (9) is laid on different equidistant sagittal plane of central shaft (8-1), and the paddle type that the stirrer paddle (9) in each plane is formed is straight leaf open turbine formula; Stirrer paddle (9) quantity on different sagittal plane equal and centrally the projection of axle (8-1) axis direction overlap.
4. house refuse sludge reduction onsite integrated apparatus as claimed in claim 2, is characterized in that: described aerobic reaction double shell (4) is made up of the first aerobic reaction cylindrical shell (4-2) and the second aerobic reacting cylinder body (4-5); Described charging aperture (4-1) is arranged at the upper one end near conveyor screw (8-2) of the first aerobic reaction cylindrical shell (4-2), described discharging opening (4-5) is arranged at the upper one end near stirrer paddle (8-3) of the second aerobic reacting cylinder body (4-5), and the first aerobic reaction cylindrical shell (4-2) is upper to be above connected by cylindrical shell connector (4-3) near one end of conveyor screw (8-2) with the second aerobic reacting cylinder body (4-5) near one end of stirrer paddle (8-3).
5. house refuse sludge reduction onsite integrated apparatus as claimed in claim 1, it is characterized in that: between the first described aerobic reaction cylindrical shell (4-2) and the second aerobic reacting cylinder body (4-5), there is difference in height, make the angle of inclination between cylindrical shell connector (4-3) and horizontal plane be 40 ° ~ 60 °.
6. house refuse sludge reduction onsite integrated apparatus as claimed in claim 1, it is characterized in that: described breaker (2) adopts double-roll crusher, and double-roll crusher comprises crushing teeth (2-3), broken chamber (2-1), travelling gear (2-2); A pair crushing toothed roller be arranged crosswise in broken chamber (2-1), and to be axially connected with travelling gear (2-2) respectively, to be rotated by the synchronized reverse drive of travelling gear, the uniform crushing teeth of axis (2-3) on crushing toothed roller.
7. house refuse sludge reduction onsite integrated apparatus as claimed in claim 6, is characterized in that: described crushing teeth (2-3) is arc inner tooth, axially uniform 8 ~ 14; Described described vibratory sieve (7) comprises flat-surfaced screen (7-1), screening bin (7-2), support pedestal (7-3), vibrating motor (7-4); Flat-surfaced screen (7-1) is in tilted layout in screening bin (7-2), and angle of inclination is 5 ° ~ 6.3 °; Vibrating motor (7-4) is placed in flat-surfaced screen (7-1) downside, 1/3rd places from the front end.
8. house refuse sludge reduction onsite integrated apparatus as claimed in claim 1, it is characterized in that: described described conveying device (3) adopts ribbon conveyer, the threephase asynchronous machine (6) that described drive unit (10) comprises reductor (5) and matches, described lifting device (1) is lift rail.
9. utilize a residents in rural community sludge reduction onsite integral treatment method for the arbitrary described device of claim 1 ~ 8, it is characterized in that, comprise the steps:
Tubbiness rubbish is promoted by dustbin lifting device (1), tilts to pour breaker (2) into and carries out broken bag break process, and the rubbish after fragmentation falls to band conveying device (3); By conveying device (3) rubbish after fragmentation is delivered to the first aerobic reaction cylindrical shell (4-2) and the second aerobic reacting cylinder body (4-5) is fermented, in the first aerobic reaction cylindrical shell (4-2) and the second aerobic reacting cylinder body (4-5) at control temperature 60 ~ 70 DEG C, utilize the yeasting that blast aeration remains aerobic, stirred by the conveying of stirring rotator (8), material is carried out layer-transferred fermentation and reduces living beings particle diameter, other impurity keeps particle diameter at 3 ~ 5cm; Material after fermentation is delivered in vibratory sieve (7) through discharging opening (4-5), carries out that material is homogeneous, removal of impurities through vibratory sieve continuous shaking.
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107282601A (en) * | 2017-07-12 | 2017-10-24 | 浙江大学 | The buried resource integrated device of house refuse decrement and its processing method |
CN107363073A (en) * | 2017-07-12 | 2017-11-21 | 浙江大学 | House refuse installation for fermenting and the resource integrated apparatus and method of decrement |
CN107377581A (en) * | 2017-07-12 | 2017-11-24 | 浙江传超环保科技有限公司 | House refuse round and device |
CN107377580A (en) * | 2017-07-12 | 2017-11-24 | 浙江传超环保科技有限公司 | House refuse is reduced method of resource and buried type integrated device |
CN112608174A (en) * | 2020-12-09 | 2021-04-06 | 南京大学 | Intestinal bionic tubular aerobic composting device, system and method |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005022883A (en) * | 2003-06-30 | 2005-01-27 | Ando Corp | Composting facility, and composting method |
CN200970594Y (en) * | 2006-10-27 | 2007-11-07 | 惠州市三峰环保设备科技有限公司 | City life garbage comprehensive treating device |
CN200978257Y (en) * | 2006-12-04 | 2007-11-21 | 天津创业环保股份有限公司 | Mixing and stirring device |
JP2009113023A (en) * | 2007-11-08 | 2009-05-28 | Mn Engineering Kk | Instantaneous extinguishing apparatus for garbage and urine |
CN201648254U (en) * | 2009-11-28 | 2010-11-24 | 天津华一有限责任公司 | Efficient aerobic fermentation treatment device |
CN203222555U (en) * | 2013-05-14 | 2013-10-02 | 天津市瑞物有机肥有限公司 | Biological organic fertilizer decomposition tank |
CN105032900A (en) * | 2015-08-19 | 2015-11-11 | 石柏军 | Integrated kitchen waste treatment equipment and method |
CN205308940U (en) * | 2015-12-23 | 2016-06-15 | 浙江大学 | Domestic waste normal position decrement integrated device |
-
2015
- 2015-12-23 CN CN201510977639.XA patent/CN105478443B/en active Active
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005022883A (en) * | 2003-06-30 | 2005-01-27 | Ando Corp | Composting facility, and composting method |
CN200970594Y (en) * | 2006-10-27 | 2007-11-07 | 惠州市三峰环保设备科技有限公司 | City life garbage comprehensive treating device |
CN200978257Y (en) * | 2006-12-04 | 2007-11-21 | 天津创业环保股份有限公司 | Mixing and stirring device |
JP2009113023A (en) * | 2007-11-08 | 2009-05-28 | Mn Engineering Kk | Instantaneous extinguishing apparatus for garbage and urine |
CN201648254U (en) * | 2009-11-28 | 2010-11-24 | 天津华一有限责任公司 | Efficient aerobic fermentation treatment device |
CN203222555U (en) * | 2013-05-14 | 2013-10-02 | 天津市瑞物有机肥有限公司 | Biological organic fertilizer decomposition tank |
CN105032900A (en) * | 2015-08-19 | 2015-11-11 | 石柏军 | Integrated kitchen waste treatment equipment and method |
CN205308940U (en) * | 2015-12-23 | 2016-06-15 | 浙江大学 | Domestic waste normal position decrement integrated device |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107282601A (en) * | 2017-07-12 | 2017-10-24 | 浙江大学 | The buried resource integrated device of house refuse decrement and its processing method |
CN107363073A (en) * | 2017-07-12 | 2017-11-21 | 浙江大学 | House refuse installation for fermenting and the resource integrated apparatus and method of decrement |
CN107377581A (en) * | 2017-07-12 | 2017-11-24 | 浙江传超环保科技有限公司 | House refuse round and device |
CN107377580A (en) * | 2017-07-12 | 2017-11-24 | 浙江传超环保科技有限公司 | House refuse is reduced method of resource and buried type integrated device |
CN107282601B (en) * | 2017-07-12 | 2018-04-20 | 浙江大学 | Buried house refuse is reduced resource integrated device and its processing method |
CN107363073B (en) * | 2017-07-12 | 2018-05-08 | 浙江大学 | House refuse installation for fermenting and the resource integrated apparatus and method of decrement |
CN107377580B (en) * | 2017-07-12 | 2023-07-18 | 浙江传超环保科技有限公司 | Household garbage reduction recycling method and buried integrated device |
CN112608174A (en) * | 2020-12-09 | 2021-04-06 | 南京大学 | Intestinal bionic tubular aerobic composting device, system and method |
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