CN106862246A - Organic solid waste comprehensive treatment equipment and technique - Google Patents
Organic solid waste comprehensive treatment equipment and technique Download PDFInfo
- Publication number
- CN106862246A CN106862246A CN201710210098.7A CN201710210098A CN106862246A CN 106862246 A CN106862246 A CN 106862246A CN 201710210098 A CN201710210098 A CN 201710210098A CN 106862246 A CN106862246 A CN 106862246A
- Authority
- CN
- China
- Prior art keywords
- waste
- waste material
- fermentation
- proportioner
- casing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 37
- 239000002910 solid waste Substances 0.000 title claims abstract description 32
- 239000002699 waste material Substances 0.000 claims abstract description 101
- 238000000855 fermentation Methods 0.000 claims abstract description 54
- 230000004151 fermentation Effects 0.000 claims abstract description 54
- 238000003860 storage Methods 0.000 claims abstract description 44
- 238000012216 screening Methods 0.000 claims abstract description 26
- 230000008569 process Effects 0.000 claims abstract description 17
- 238000012544 monitoring process Methods 0.000 claims abstract description 13
- 238000012545 processing Methods 0.000 claims abstract description 10
- 238000007599 discharging Methods 0.000 claims abstract description 5
- 230000000694 effects Effects 0.000 claims abstract description 3
- 239000000463 material Substances 0.000 claims description 45
- 238000009423 ventilation Methods 0.000 claims description 39
- 239000000523 sample Substances 0.000 claims description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 33
- 239000002921 fermentation waste Substances 0.000 claims description 28
- 238000002156 mixing Methods 0.000 claims description 13
- 239000010802 sludge Substances 0.000 claims description 13
- 244000144972 livestock Species 0.000 claims description 10
- 239000007789 gas Substances 0.000 claims description 8
- 230000006641 stabilisation Effects 0.000 claims description 5
- 238000011105 stabilization Methods 0.000 claims description 5
- 230000029087 digestion Effects 0.000 claims description 2
- 238000003780 insertion Methods 0.000 claims 1
- 230000037431 insertion Effects 0.000 claims 1
- 230000033228 biological regulation Effects 0.000 abstract description 3
- 241000196324 Embryophyta Species 0.000 description 21
- 239000002689 soil Substances 0.000 description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 11
- 229910052799 carbon Inorganic materials 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 238000005498 polishing Methods 0.000 description 7
- 238000010586 diagram Methods 0.000 description 6
- 238000012546 transfer Methods 0.000 description 6
- 230000007306 turnover Effects 0.000 description 6
- 230000008859 change Effects 0.000 description 4
- 230000003750 conditioning effect Effects 0.000 description 4
- 238000010276 construction Methods 0.000 description 4
- 238000001514 detection method Methods 0.000 description 4
- 239000011159 matrix material Substances 0.000 description 4
- 230000007704 transition Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000003895 organic fertilizer Substances 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 238000013459 approach Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000005842 biochemical reaction Methods 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 238000009395 breeding Methods 0.000 description 2
- 230000001488 breeding effect Effects 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 239000002361 compost Substances 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 230000000249 desinfective effect Effects 0.000 description 2
- 238000005553 drilling Methods 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000010813 municipal solid waste Substances 0.000 description 2
- 230000035764 nutrition Effects 0.000 description 2
- 235000016709 nutrition Nutrition 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 230000008439 repair process Effects 0.000 description 2
- 239000003516 soil conditioner Substances 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 230000000007 visual effect Effects 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- 206010000060 Abdominal distension Diseases 0.000 description 1
- 241000208340 Araliaceae Species 0.000 description 1
- 241000209202 Bromus secalinus Species 0.000 description 1
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 description 1
- 235000003140 Panax quinquefolius Nutrition 0.000 description 1
- 239000002671 adjuvant Substances 0.000 description 1
- 238000010564 aerobic fermentation Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 208000024330 bloating Diseases 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000002781 deodorant agent Substances 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 235000008434 ginseng Nutrition 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000009270 solid waste treatment Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
Classifications
-
- 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
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Disclose a kind of organic solid waste comprehensive treatment equipment and technique.Wherein, the equipment includes multiple storage bins, first mixer, proportioner, fermenting case and screening plant, charging aperture of multiple storage bins respectively with the first mixer is connected, for the pending waste material of storage of classifying, the discharging opening of the first mixer is connected with proportioner, the discharge end of proportioner is connected with the feed end of fermenting case, the discharge end of fermenting case is connected with the discharge end of screening plant, wherein, proportioner receives Various Wastes, Various Wastes include the waste material from the first mixer, after proportioner is added in proportion to the various waste materials for receiving, fermenting case is transported to be fermented, the waste material of completion fermentation is transported to screening plant carries out screening process.The equipment and technique can realize that organic solid waste can be realized the automatic high-efficiency operation of links in processing procedure, and effective monitoring and in time regulation are carried out to waste fermentation process, substantially increase treatment effeciency and treatment effect.
Description
Technical field
The present invention relates to organic solid waste comprehensive treatment technique field, more particularly, to a kind of organic solid waste integrated treatment
Equipment and technique.
Background technology
Organic solid waste is processed and is made in the native nature of input again of organic carbon, realized that refuse reclamation is one new
Emerging technology.And in the process, fermentation is a most key link.
Existing organic solid waste Zymolysis Equipment, integration and intelligence degree are poor, it is impossible to effective Monitoring and Controlling hair
Ferment environment.Also, existing Zymolysis Equipment can not effectively complete pretreatment, sorting, the preparation to organic solid waste waste material so that
Operation is in disorder numerous and diverse.In consideration of it, existing organic solid waste Zymolysis Equipment causes that material fermentation process is sluggish or it is insufficient to ferment,
Also so that the technological process to solid waste integrated treatment is difficult to control to that satisfactory organic carbon soil can not be made.
The content of the invention
In view of this, it is existing to solve it is an object of the invention to provide a kind of organic solid waste comprehensive treatment equipment and technique
There is problem present in technology.
According to the first aspect of the invention, there is provided a kind of organic solid waste comprehensive treatment equipment, including multiple storage bins, first
Mixer, proportioner, fermenting case and screening plant, multiple storage bins connect with the charging aperture of first mixer respectively
Connect, for the pending waste material of storage of classifying, the discharging opening of first mixer is connected with the proportioner, the dispensing dress
The discharge end put is connected with the feed end of the fermenting case, and the discharge end of the fermenting case connects with the discharge end of the screening plant
Connect,
Wherein, the proportioner receives Various Wastes, and the Various Wastes include useless from first mixer
Material, after the proportioner is added in proportion to the various waste materials for receiving, is transported to the fermenting case and is fermented, complete
Waste material into fermentation is transported to the screening plant and carries out screening process.
Preferably, the fermenting case includes temperature compensation system, casing and chain scraper conveyor, and the chain scraper conveyor is located at
In the casing, for carrying and fermentation waste is conveyed, the temperature compensation system collection solar energy and after being converted into heat energy
Heat energy is divided two-way and selected the waste material in the casing is heated all the way at least within,
Wherein, heat energy is transported to fermentation waste by the first via through the outer wall of the casing, and fermentation waste is heated, the
Two tunnels directly convey heat energy through the mode of air blast to the waste material.
Preferably, the temperature compensation system includes solar heat-collection plate and water tank, and the solar heat-collection plate is used to receive
Collection solar energy is simultaneously converted into heat energy to the water heating in the water tank, and the hot water circuit in the water tank forms the first temperature control branch
Road and the second temperature control branch road, hot water in the water tank is selectable to flow through the first temperature control branch road and the second branch road at least
One of them,
Wherein, the heat on the first temperature control branch road is used to be delivered to fermentation waste to heat energy through the outer wall of the casing
In, the heat on the second temperature control branch road is used for the mode through air blast to the logical hot blast of waste material in the casing.
Preferably, the pipeline of the second temperature control branch road is provided with least one heat-sink unit, the second temperature control branch road
Pipeline pass through the heat-sink unit,
The heat-sink unit include shell and the radiating fin in the shell, the shell have first port and
Second port, the first port is connected with the first blower fan, and the second port is used to discharge hot blast.
Preferably, each carrier bar of the chain scraper conveyor has ventilated cavity, and the first table perpendicular to one another respectively
Face and second surface, offer multiple fresh air inlets for extending to the ventilated cavity on the first surface, for by outside
Wind is passed through the ventilated cavity；
The second surface is provided with multiple ventilation plugs, and is connected with the ventilated cavity, for the closed vented cavity
Room, and the air-flow in the ventilated cavity is released.
Preferably, the second surface is provided with mounting hole, for installing the ventilation plug；
The outlet air end of the ventilation plug is provided with primary diaphragm, and the primary diaphragm includes multiple diaphragm valves, multiple films
The outward flange of piece valve is individually fixed in the outlet air end of the ventilation plug, slitless connection between inside edge, so as to go out described in closed
Wind end,
The air intake of the ventilation plug is provided with secondary diaphragm, multiple current stabilization holes is offered on the secondary diaphragm, for steady
Determine air-flow.
Preferably, the fermenting case also include monitoring system, the casing built with fermentation waste, the monitoring system bag
Drive device and at least one probe being fixed in the drive device are included, the drive device is slidably secured institute
State on the inwall of casing, the drive device is used to drive the probe movement, so as to detect diverse location in the casing
Waste material, and drive it is described probe move up and down by it is described probe insert waste material in or depart from waste material.
Preferably, the storage bin includes the first storage bin, the second storage bin, the 3rd storage bin, the 4th storage bin, its
In,
First storage bin is used for temporary livestock waste material of dying of illness, and second storage bin is useless for keeping in kitchen sorting
Material, the 3rd storage bin is used to keep in municipal sludge waste material, and the 4th storage bin is used to keep in plant's excrement waste material.
According to the second aspect of the invention, there is provided a kind of organic solid waste comprehensive processing technique, comprise the following steps：
A), will die of illness livestock waste material, kitchen sorting waste material, that municipal sludge waste material and plant's excrement carry out waste material difference is defeated
Deliver to the first mixer to be mixed, form mixing waste；
B) mixing waste, is delivered to proportioner, and through the proportioner by the mixing waste, auxiliary material and
Return to material to be added in proportion, form proportioning waste material；
C) the proportioning waste material, is delivered into fermenting case to be fermented, screening plant is delivered to after the completion of fermentation and is sieved
Point；
D), remaining waste material continues to return to the proportioner on the screening plant, is processed again.
Preferably, it is described proportioning waste material sequentially passed through in the fermenting case high temperature fermentation stage, the mesophilic digestion stage and
The cold fermentation stage, wherein,
In the high temperature fermentation stage, when the temperature in fermentation waste is more than preset temperature, start-up temperature compensation system
Release cold wind, and waste material is stirred.
Beneficial effect：
The organic solid waste comprehensive treatment equipment and technique provided according to the present invention, can realize being transported outside organic carbon soil finished product
Row recycling.Organic carbon soil can as matrix and soil conditioner be directly used in lawn, flowers, wasteland, seedling medium,
Nursery, ornamental plant, turf, meadow, park, highway greenbelt and golf course and tailing heap, stone pit, outdoor coal
That cheats reclaims, it is also possible to the overburden soil as refuse landfill.Due to the daily Nutrition Soil quantity for producing less, by production
The approach such as soil matrix, organic fertilizer can dissolve, therefore its final outlet has no problem.
This organic solid waste comprehensive processing technique mechanical automation degree is higher, with high-seal system and vent gas treatment
System can avoid pollution of the waste gas (NH3, H2S) produced in fermentation process to environment, in fermentation biochemical reaction process, favorably
In the growth and breeding of oxygen supply, mass transfer, heat transfer and microorganism, the speed of microbial degradation organic matter is accelerated, effectively reduced
Fermentation period, can be reduced investment outlay, and disposal ability can be improved again.Always have it is following some：
1) deodoring and disinfecting ability is strong, totally-enclosed system, it is to avoid the pollution of fermentation odor NH3, H2S to environment；Can be real
Now dying of illness, livestock, agricultural abandoned stalk, kitchen garbage be innoxious, disposal of resources；
2) floor space is small, the treating capacity of 30t/d, and the total floor space of engineering is 2600m2；
3) flow is short, and the construction period is short, and 30t/d throughput engineerings most 6 months can Construction Acceptance；
4) operating cost is low, and this process sludge treatment totle drilling cost is 200 yuan/ton of mud；
5) interlocking joint control is realized in oxygen content, temperature, ventilation, carrier bar braking, can in time be monitored and be adjusted according to change condition
Whole technological parameter；
6) simple system reliability, a little repair is capable of achieving the integrated management with sludge dewatering system, reduces management and people
Member's burden；
7) main reaction system is divided into high, medium and low three sections disposable fermentation reactions, it is not necessary to secondary compost, shortens whole hair
The ferment cycle；
8) solar energy temperature compensation system is used, it is to avoid the temperature difference influence of season and region, it is ensured that the stabilization of reaction
Property and high efficiency.
Brief description of the drawings
By description referring to the drawings to the embodiment of the present invention, of the invention above-mentioned and other purposes, feature and
Advantage will be apparent from.
Fig. 1 is the structural representation of the organic solid waste comprehensive treatment equipment according to the embodiment of the present invention.
Fig. 2 is the structural representation of the proportioner according to the embodiment of the present invention.
Fig. 3 is the front view of the fermenting case according to the embodiment of the present invention.
Fig. 4 is the A-A sectional views of Fig. 3.
Fig. 5 is the B-B sectional views of Fig. 3.
Fig. 6 is the combination schematic diagram of temperature compensation system according to the embodiment of the present invention and casing.
Fig. 7 is the combination schematic diagram of the temperature compensation system according to the embodiment of the present invention.
Fig. 8 is the split-type structural schematic diagram of the carrier bar for being provided with ventilation plug according to the embodiment of the present invention.
Fig. 9 is the structural representation of the carrier bar for being provided with ventilation plug according to the embodiment of the present invention.
Figure 10-11 is the carrier bar dimensional structure diagram of the different visual angles according to the embodiment of the present invention.
Figure 12-13 is the dimensional structure diagram of the ventilation plug of the different visual angles according to the embodiment of the present invention.
Figure 14 is the sectional view of the carrier bar of the ventilation plug according to the embodiment of the present invention.
Figure 15 is the attachment structure schematic diagram between the carrier bar according to the embodiment of the present invention.
Figure 16 is the flow chart of the organic solid waste comprehensive processing technique according to the embodiment of the present invention.
In figure：First storage bin 11, the second storage bin 12, the 3rd storage bin 13, the 4th storage bin 14, proportioner 2,
Two conveyers 21, the first hopper 22, the second hopper 23, the 3rd hopper 24, fermenting case 3, screening plant 4, the first conveyer 51,
It is one mixer 52, the second mixer 53, temperature compensation system 31, solar heat-collection plate 311, water tank 312, heating coil 313, outer
Shell 3151, first port 3152, second port 3153, radiating fin 3154, temperature conditioning unit 316, water pump 317, the first blower fan
3181st, the second blower fan 3182, the first valve 3191, the second valve 3192, casing 32, charging aperture 321, exhaust collection mouthfuls 322, the
One limiting plate 323, the second limiting plate 324, chain scraper conveyor 33, carrier bar 331, fresh air inlet 3311, mounting hole 3312, ventilation plug
332nd, boss 3321, diaphragm valve 3322, butted line 3323, current stabilization hole 3324, chain 333, duct 300, turn over polishing apparatus 34, rotating shaft
341st, the 614, first electric pushrod of probe of the 612, the 3rd probe of throwing rod 342, first the 611, second probe of probe the 613, the 4th is turned over
621st, transition block 622, the second electric pushrod 623, chute 63, leading screw 64, sliding block 65, mounting disc 66, controller 67, support 7, drum
Air port 8.
Specific embodiment
Various embodiments of the present invention are more fully described hereinafter with reference to accompanying drawing.In various figures, identical element
Represented using same or similar reference.For the sake of clarity, the various pieces in accompanying drawing are not necessarily to scale.
As shown in figure 1, various organic waste materials can be carried out at treatment by the organic solid waste comprehensive treatment equipment that the present invention is provided
Reason, is made organic carbon soil and puts into natural environment again, is circulated recycling.The organic solid waste comprehensive treatment equipment includes multiple
Storage bin, the first mixer 52, proportioner 2, fermenting case 3 and screening plant 4.Multiple storage bins are respectively with described first
The charging aperture 321 of mixer 52 is connected, for the pending waste material of storage of classifying, the discharging opening of first mixer 52 with it is described
Proportioner 2 is connected, the discharge end of the proportioner 2 is connected with the feed end of the fermenting case 3, and the fermenting case 3 goes out
Material end is connected with the discharge end of the screening plant 4.
Wherein, the proportioner 2 receives Various Wastes, and the Various Wastes are included from first mixer 52
Waste material, after the various waste materials of 2 pairs of receptions of the proportioner are added in proportion, are transported to the fermenting case 3 and are sent out
Ferment, the waste material of completion fermentation is transported to the screening plant 4 carries out screening process.
The storage bin includes the first storage bin 11, the second storage bin 12, the 3rd storage bin 13, the 4th storage bin 14.Its
In, first storage bin 11 is used for temporary livestock waste material of dying of illness, and second storage bin 12 is used to keep in kitchen sorting waste material,
3rd storage bin 13 is used to keep in municipal sludge waste material, and the 4th storage bin 14 is used to keep in plant's excrement waste material.
The first conveyer 51 is provided between each storage bin and the first mixer 52, for the material in storage bin to be conveyed
To the first conveyer 51.
As shown in Fig. 2 proportioner 2 includes second conveyor 21 and multiple hoppers, multiple hoppers are located at second conveyor
21 top, for leaking waste material about 21 to second conveyor.In the embodiment, three hoppers are provided with altogether, including along second
The first hopper 22, the second hopper 23 and the 3rd hopper 24 that the direction of transfer of conveyer 21 is arranged successively, are respectively used to lower leakage not
Generic waste material.Wherein, the first hopper 22, the second hopper 23 and the 3rd hopper 24 are respectively used to lower leakage and need to be processed again
Return material, the first mixer 52 conveying mixing waste and auxiliary material.The auxiliary material waste material such as including stalk and saw foam.Each hopper
Valve plate is provided with, for controlling the lower leakage speed of waste material in hopper, so that three kinds of mass ratios of waste material in fermentation waste are controlled,
Form proportioning waste material.After the material of three kinds of certain proportion relations is fallen on second conveyor 21, it is delivered to by second conveyor 21
Fermenting case 3.
Further, the second mixer 53 can be set between fermenting case 3 and second conveyor 21, and second conveyor 21 is first
Proportioning waste material is first delivered to the second mixer 53, being delivered to fermenting case 3 after being mixed again carries out fermentation process.Such as Fig. 3-7
Shown, fermenting case 3 includes temperature compensation system 31, casing 32 and chain scraper conveyor 33.The chain scraper conveyor 33 is located at described
In casing 32, for carrying and fermentation materials are conveyed, the collection solar energy of the temperature compensation system 31 and after being converted into heat energy
Heat energy is divided two-way and selected the fermentation materials in the casing 32 are heated all the way at least within.Wherein, the first via is through institute
Heat energy is transported to fermentation materials by the outer wall for stating casing 32, and fermentation materials are heated, and the second tunnel is direct through the mode of air blast
Heat energy is conveyed to the material.Be provided with casing 32 and turn over polishing apparatus 34, its number is multiple, turned over described in multiple polishing apparatus 34 along
The length direction arrangement of the casing 32.Turn over polishing apparatus 34 and turn over throwing rod including rotating shaft 341 and the multiple in the rotating shaft 341
342, turn over polishing apparatus 34 and be perpendicularly fixed at casing 32 along on width through rotating shaft 341, i.e., with the transmission of chain scraper conveyor 33
Direction is vertical.In the embodiment, four being provided with altogether and turning over polishing apparatus 34, each turns over polishing apparatus 34 and can independently drive, and can also drive simultaneously
It is dynamic.Material is in course of conveying by turning over throwing, it is possible to increase different material, such as so as to increase the contact between sludge and stalk
Area, so as to increase heap body voidage, makes fermentation reaction more abundant, so do not need substantial amounts of stalk to be used as support, greatly
Reduce processing cost greatly.
Be provided with charging aperture 321 above the first end alongst of the casing 32, the charging aperture 321 with it is described
The connection of the inside of casing 32.The top of the casing 32 is provided with exhaust collection mouthful 322 away from one end of the discharging opening, for collecting
State the gas that fermentation is produced in casing 32.The casing 32 along being provided with the first limiting plate 323 in the first end of its length direction,
The mobilizable casing 32 that is installed on of first limiting plate 323 enters institute along on the inwall of width for control
State the inventory on chain scraper conveyor 33.The casing 32 along being provided with the second limiting plate 324 in the second end of its length direction,
The mobilizable casing 32 that is installed on of second limiting plate 324 flows out institute along on the inwall of width for control
State the inventory on chain scraper conveyor 33.In the embodiment, the first limiting plate 323 and the second limiting plate 324 are distinguished height and are adjusted
That saves is installed on the inwall of casing 32, and by adjusting between limiting plate lower end and the upper strata carrier bar 331 of chain scraper conveyor 33
Distance controls inlet amount or load.
Temperature compensation system 31 is used for casing 32, carries out temperature control.The temperature compensation system 31 includes solar energy collection
Hot plate 311 and water tank 312, the solar heat-collection plate 311 are used to collect solar energy and be converted into heat energy to the water tank 312
In water heating, hot water circuit in water tank 312 forms the first temperature control branch road and the second temperature control branch road, in the water tank 312
Hot water is selectable flow through the first temperature control branch road and the second branch road at least one.It is provided with the water tank 312 and is added
Hot coil 313, two ports of the heating coil 313 connect with two ports of the solar heat-collection plate 311 respectively, shape
Into hot gas cycle passage.
Wherein, the heat on the first temperature control branch road is used to heat the outer wall of casing 32, second temperature control
Heat on branch road is used for the mode through air blast to internal logical hot blast in the case.
The first temperature control branch road is provided with multiple temperature conditioning units 316 being sequentially connected in series, for the casing 32 to incubator
Outer wall is heated, so that the temperature in control cabinet.The temperature conditioning unit 316 elects fin as, and will be flowed through by fin
The heat of the hot water of one temperature control branch road is distributed and is uniformly dispersed into casing 32.By the side heated to the outer wall of casing 32
Formula, can be used as carrying out temperature controlled basic mode of heating to casing 32.
The pipeline of the second temperature control branch road is provided with heat-sink unit.In the embodiment, the number of heat-sink unit is one,
The pipeline of the second temperature control branch road passes through the heat-sink unit.The heat-sink unit includes shell 3151 and located at the shell
Radiating fin 3154 in 3151.The shell 3151 has first port 3152 and first port described in second port 3153
3152 connect with the first blower fan 3181, and the second port 3153 is used to discharge hot blast.Flow through the second temperature control bypass line
Hot water, when heat-sink unit is flowed through, transfers heat to radiating fin 3154.When the first blower fan 3181 starts, by outside wind
It is blasted into the shell 3151 of heat-sink unit, and flows through radiating fin 3154, the heat that hot water is distributed is taken away, and through shell
3151 second port 3153 is blown out to the bottom blast mouthful 8 of casing 32.Blast orifice 8 is defeated located at the carrier bar that the inside of casing 32 is set
Send between the upper strata carrier bar 331 of machine 33 and lower floor's carrier bar 331, the hot blast for bloating of air blower is through the adjacent carrier bar of upper strata carrier bar 331
Gap between 331 enters in the fermentation materials that upper strata carrier bar 331 is carried.Because the mode of air blast can quickly send hot blast
In entering fermentation materials, so that the temperature of quick regulation fermentation materials, it is ensured that the temperature environment needed for material fermentation.
Specifically, the water outlet in water tank 312 is provided with water pump 317, for providing power by the circulation of hot water.Along heat
The flow direction of water, was provided with the first valve 3191, in the second bypass duct before multiple temperature conditioning units 316 on tie point pipeline
The second valve 3192 is provided with road before heat-sink unit.Coordinated by the unlatching of the first valve 3191 and the second valve 3192, come
It is selectable to open one of the first temperature control branch road and the second temperature control branch road, so as to select to casing according to actual needs
32 heating location.
Preferably, the first blower fan 3181 elects servo blower fan as, in order to carry out to adjust at any time fermentation temperature as needed
Degree, realization is fine-tuned to temperature controlled.
Further, second blower fan can be set between the second port 3153 of heat-sink unit shell 3151 and blast orifice 8
3182, to prevent from influenceing the transporting velocity of hot blast because blowing line is long.The number of the second blower fan 3182 can for one or
Person is the multiple being sequentially connected in series, and its specific number sets as needed.In the embodiment, the number of the second blower fan 3182 is two
It is individual.
The temperature compensation system 31, due to being provided with the first temperature control branch road and the second temperature control branch road, in fermentation waste process
In, air blast in casing 32 can be heated or be directly toward in the selection outer wall of casing 32 according to actual needs, so that will be to case
The temperature control mode of body 32 is set to the pattern that basic mode of heating and quick regulation mode are engaged, can be more accurate quickly real
Now to the control of fermentation waste temperature environment.On the other hand, heating is carried out to water as to case using solar heat-collection plate 311
The temperature control thermal source of body 32, can provide temperature control heat, fermentation costs using natural resources.
In the embodiment, design casing 32 size is (x x wide long are high) 45mx4mx3.8m, volume 684m3, bank in case
Body section (x wide is high) 3mx1.5m, casing 32 uses stainless steel, and interior crawler belt translational speed is 1-10m/h in case.Use liquid
Pressure transmission system, the on the one hand matching beneficial to technological parameter is adjusted, and on the other hand can be effectively accomplished the effect of energy-conservation, is reduced
Processing cost.It is 30t/d according to total treating capacity is designed, fermentation period most long is 15 days, low boy cabinet 32 is used as being an independence
Reactor, interior part along casing 32 length direction, and along the fermentation waste conveying direction of chain scraper conveyor 33, by ventilation
High temperature section, middle-temperature section and low-temperature zone are set to, wherein high temperature section fermentation time is 3-5 days, and length is cylinder 1/4, and middle low temperature is
It is continuous overall, in 10-15 days overall reaction cycle, account for barrel lenght 3/4.Further, fermenting case 3 also includes monitoring system.Should
Monitoring system includes drive device and the probe being fixed in drive device, and drive device is slidably secured casing 321
Inwall on, drive device be used for drive probe movement, so as to detect the fermentation waste of diverse location in casing 321, and drive
Probe is moved up and down and inserts a probe into fermentation waste or depart from fermentation waste.
In order to realize the detection to fermentation waste multiple parameters index in casing 32, probe includes multiple probes, and multiple is visited
Head is respectively used to detect different parameters index.In the embodiment, the specific number of probe is four, specifically includes the first probe
611st, the probe 613 of the second probe the 612, the 3rd and the 4th probe 614.Wherein, the first probe 611 is used to detect oxygen in fermentation waste
Gas parameter index, the first probe 611 is used for volatilization gas parameter index in fermentation waste, and the 3rd probe 613 is used for detection and ferments
The index parameter of the pH value of waste material.
Drive device includes the first electric pushrod 621, the electric pushrod 623 of transition block 622 and second.First electric pushrod
621 flexible rod end is fixedly connected with transition block 622, and bar cylinder end is with slidable on the madial wall of casing 321, and second is electric
The bar cylinder end of dynamic push rod 623 is fixedly connected with transition block 622, and flexible rod end is connected with multiple probe.On the madial wall of casing 32
The leading screw 64 for being provided with and extending along chute 63 is provided with chute 63, chute 63, and the barrel end outer wall of the first drive rod is provided with
Sliding block 65, the cylinder of the first drive rod is located on the leading screw 64 in chute 63 through its sliding block 65.The level of first electric pushrod 621 sets
Put, the second electric pushrod 623 is vertically arranged.Drive device also includes mounting disc 66, and mounting disc 66 is provided with multiple for installing
The mounting hole 3312 of probe, multiple probe is respectively arranged in corresponding mounting hole 3312, and is fixed on driving through mounting disc 66
Monitoring system also includes controller 676 on device, and controller 67 elects PLC as, and it is electrically connected with probe, for receiving from each
The detectable signal of individual probe, and by signal analysis and processing.
During the fermentation, monitoring system monitors the parameters index in fermentation waste at any time as needed.During monitoring,
Leading screw 64 is rotated first, is slided along the length direction of casing 32 with movable slider 65, selectes approximate location to be detected.Then,
First electric pushrod 621 stretches, and completes Detection location.Then, the second electric pushrod 623 is overhanging, drives multiple probes to decline simultaneously
It is inserted into fermentation waste, the parameters index to fermentation waste is detected.After the completion of detection, the second electric pushrod 623
Retraction, drives multiple probes to rise to the top of fermentation waste.
The monitoring system can in time monitor the indices ginseng of the fermentation waste of each position casing 32 Nei as needed
Number such that it is able to which grasp promptly and accurately simultaneously controls the yeasting of fermentation waste, and then improve fermentation efficiency, and makes to ferment
Journey is thorough.As shown in figures 8 to 15, each carrier bar 331 of the second conveyor 21 of carrier bar 331 has ventilated cavity, and perpendicular to one another
First surface and second surface, multiple fresh air inlets for extending to the ventilated cavity are offered on the first surface
3311, for outside wind to be passed through into the ventilated cavity.Multiple ventilation plug 332 is respectively arranged on the second surface, and with institute
Ventilated cavity connection is stated, for the closed ventilated cavity, and the air-flow in the ventilated cavity is released.
In the embodiment, carrier bar 331 is made up of rectangle pipe material, and its two ends is sealed, such as by rectangular tube
The both-side opening end welded blank of material realizes sealing.In this way, being internally formed ventilated cavity in carrier bar 331.The second of the carrier bar 331
Surface is provided with mounting hole 3312, for installing the ventilation plug 332.Mounting hole 3312 is shoulder hole, for blocking ventilation plug
332。
In the embodiment, ventilation plug 332 is made up of the material with certain elasticity, such as rubber.Ventilation plug 332 is ladder
Column structure, the periphery of ventilation 332 air intakes of plug is provided with boss 3321.The geomery and mounting hole 3312 of ventilation plug 332
Match.Specifically, the big end of ventilation plug 332, i.e. diameter of the diameter of boss 3321 slightly larger than mounting hole 3312 so that ventilation plug
332 can be clamped in mounting hole 3312 through its big end.The height at the big end of ventilating opening is less than or equal to the depth of mounting hole 3312, with
Just so that the big end of ventilation plug 332 is contained in mounting hole 3312, flowed out from ventilated cavity in order to gas.
The outlet air end of the ventilation plug 332 is provided with primary diaphragm, and the primary diaphragm includes multiple diaphragm valves 33222, many
The outward flange of the individual diaphragm valve 3322 be individually fixed in it is described ventilation plug 332 outlet air end, slitless connection between inside edge,
So as to the closed outlet air end.In the embodiment, there are three diaphragm valves 3322, three diaphragm valves 3322 altogether on ventilation plug 332
Butted line 3323 between inside edge is three straight lines outwards dissipated from a point, is each other 120 ° between three straight lines
Angle.The butted line 3323 cleaved can be formed.The concrete shape of the butted line 3323 can set as needed.Work as ventilation
When wind in chamber reaches certain pressure, primary diaphragm is just distinguished into certain interval from butted line 3323, and flow out from gap.
Secondary diaphragm is provided with the air intake of the ventilation plug 332, multiple current stabilization holes are offered on the secondary diaphragm
3324, for steady air flow.Connected through duct 300 between air intake and outlet air end.
In the present embodiment, only it is sequentially connected that the attachment structure between carrier bar 331 is shown with three blocks of carrier bars 331, and not
The chain scraper conveyor 33 only has three blocks of carrier bars 331.When carrier bar 331 is used, multiple connecting plate components are connected through chain 333, shape
Into closed loop configuration, and surround and support on the support 7 of chain scraper conveyor 33.Wherein, the first surface direction of each carrier bar 331
The inside of closed loop configuration.Specifically, one group of chain 333 can respectively be set at the two ends of each connected carrier bar 331, i.e., two are set altogether
Group chain 333.
Using the second conveyor 21 of carrier bar 331 of the carrier bar 331, can be used to convey fermentation materials, such as it is comprehensive located at solid waste
Treatment is closed to be formed in the fermenting case 3 of organic carbon soil.When needing to air is blasted in fermenting case 3, from the second conveyor of carrier bar 331
The bottom of 21 upper strata carrier bars 331 blasts air stream, and fresh air inlet 3311 of the air stream from the first surface of each carrier bar 331 enters
In the vent passages of each carrier bar 331, then by the second surface of carrier bar 331 ventilation plug 332 enter adjacent carrier bar 331 it
Between gap in, in then flowing upwardly into fermentation materials from the gap between carrier bar 331, realize ventilation to fermentation materials and note
Oxygen.
Because ventilation plug 332 is provided with primary diaphragm, ventilation diaphragm under certain wind-force, can from each diaphragm valve 3322 it
Between butted line 3323 at open, so as to the wind in ventilated cavity be bloated.During wind in by ventilated cavity is bloated,
Because the aperture slots of primary diaphragm are smaller, the solidliquid mixture flowed out in fermentation materials will not enter vented cavity from the first template
Room.
Due to there is ventilation plug 332 on carrier bar 331, while realizing divulging information fermentation materials, fermentation materials are prevented from
In solidliquid mixture obstruction air outlet, inside carrier bar 331, thus ensure ventilation fluency.
As shown in figure 16, when being processed debirs using the organic solid waste comprehensive treatment equipment in the present embodiment,
Using following steps, with specific reference to step S01-S02.
In step S01, the livestock waste material that will die of illness, kitchen sorting waste material, municipal sludge waste material and plant's excrement are carried out
Waste material is delivered to the first mixer 52 and is mixed respectively, forms mixing waste.
Specifically, it is (aqueous that livestock waste material, the kitchen of dying of illness first sort waste material, municipal sludge waste material and plant's excrement
Rate about 80%), the organic adjuvants (moisture content 20%) such as agriculture waste stalk and return to material (moisture content 40%) by the first conveyer
51 are delivered to the first mixer 52 is mixed, new city mixing waste.Wherein, kitchen sorting waste material need to be by sorting, crushing, removing
Oil, desalination etc. pre-process measure；Livestock waste material of dying of illness need to be pre-processed by measures such as crushing, high-temperature sterilizations, subsequently into
Zymolysis Equipment；The waste material such as excrement and sludge need to adjust its moisture content and be adjusted to 80% or so.
In step S02, the mixing waste is delivered to proportioner 2, and through the proportioner 2 by the mixing
Waste material, auxiliary material and return material are added in proportion, form proportioning waste material.
Specifically, in the second hopper 23 mixing waste in step S01 being delivered on proportioner 2, and adjust right
The aperture size of the respective valve of the corresponding first to the 3rd hopper 24 is answered, so as to the mixing waste, auxiliary material and return material be pressed
According to certain weight ratio through being fallen on second conveyor 21 under respective hopper, the proportioning material that formation is proportionally prepared.
In step S03, the proportioning waste material is delivered to fermenting case 3 and is fermented, screening is delivered to after the completion of fermentation
Device 4 is sieved.
Specifically, the proportioning material prepared in step S02 is delivered to the second mixer 53, is mixed through the second mixer 53
Afterwards, fermenting case 3 is delivered to be fermented.The use of air blower is heap body oxygen supply in fermentation process, ferments initial stage, aerobic microbiological
Rapid propagation, heap temperature is raised rapidly, and after fermentation in 2-3 days enters the megathermal period.By integral intelligent aerobic fermentation equipment certainly
Dynamic monitoring and control system control fermentation heap body is maintained more than 5-7 days in 50 DEG C~70 DEG C of hot stage, is fully killed with reaching
Go out pathogen and weed seed, realizes the innoxious and stabilized purpose of material.After megathermal period terminates, using multi-functional and right
Material carry out it is even turn over, the material of diverse location is uniformly mixed, improve fermented product quality.
Fermentation completion forms organic carbon soil, and organic carbon soil is delivered into screening plant 4, carries out screening process.
In step S04, remaining waste material continues to return to the proportioner 2 on the screening plant 4, is located again
Reason.
Specifically, screening plant 4 is specially rotary screen, and its screen-aperture size of the embodiment is 3mm, less than screen-aperture
Under drain to the bottom of rotary screen, after packing, form organic fertilizer and again return to the Nature, reused.Stay in rolling
The bulky grain organic carbon soil on shaft screen top carries out the first hopper 22 of proportioner 2 again as material is returned.
During the fermentation, fermenting case 3 is the structure of totally-enclosed, and foul smell will not be escaped to outside equipment, meanwhile, match somebody with somebody in equipment
There is deodoration system, the foul smell produced in fermentation process is delivered in deodorant built-in deodorizing device and is processed in real time, makes generation
Foul smell processed in time, it is ensured that the environmental quality on plant area periphery.
Organic carbon soil finished product outward transport carries out recycling.Organic carbon soil can directly be used as matrix and soil conditioner
In lawn, flowers, wasteland, seedling medium, nursery, ornamental plant, turf, meadow, park, highway greenbelt and golf
Court and tailing heap, stone pit, outdoor coalpit are reclaimed, it is also possible to the overburden soil as refuse landfill.Due to producing daily
Raw Nutrition Soil quantity less, can be dissolved by producing the approach such as soil matrix, organic fertilizer, therefore its final outlet is not asked
Topic.
This organic solid waste comprehensive processing technique mechanical automation degree is higher, with high-seal system and vent gas treatment
System can avoid pollution of the waste gas (NH3, H2S) produced in fermentation process to environment, in fermentation biochemical reaction process, favorably
In the growth and breeding of oxygen supply, mass transfer, heat transfer and microorganism, the speed of microbial degradation organic matter is accelerated, effectively reduced
Fermentation period, can be reduced investment outlay, and disposal ability can be improved again.Always have it is following some：
1) deodoring and disinfecting ability is strong, totally-enclosed system, it is to avoid the pollution of fermentation odor NH3, H2S to environment；Can be real
Now dying of illness, livestock, agricultural abandoned stalk, kitchen garbage be innoxious, disposal of resources；
2) floor space is small, the treating capacity of 30t/d, and the total floor space of engineering is 2600m2；
3) flow is short, and the construction period is short, and 30t/d throughput engineerings most 6 months can Construction Acceptance；
4) operating cost is low, and this process sludge treatment totle drilling cost is 200 yuan/ton of mud；
5) interlocking joint control is realized in oxygen content, temperature, ventilation, the braking of carrier bar 331, can be monitored in time simultaneously according to change condition
Adjusting process parameter；
6) simple system reliability, a little repair is capable of achieving the integrated management with sludge dewatering system, reduces management and people
Member's burden；
7) main reaction system is divided into high, medium and low three sections disposable fermentation reactions, it is not necessary to secondary compost, shortens whole hair
The ferment cycle；
8) using solar energy temperature compensation system 31, it is to avoid the temperature difference influence in season and region, it is ensured that reaction it is steady
Qualitative and high efficiency.
It should be noted that herein, such as first and second or the like relational terms are used merely to a reality
Body or operation make a distinction with another entity or operation, and not necessarily require or imply these entities or deposited between operating
In any this actual relation or order.And, term " including ", "comprising" or its any other variant be intended to
Nonexcludability is included, so that process, method, article or equipment including a series of key elements not only will including those
Element, but also other key elements including being not expressly set out, or also include being this process, method, article or equipment
Intrinsic key element.In the absence of more restrictions, the key element limited by sentence "including a ...", it is not excluded that
Also there is other identical element in process, method, article or equipment including the key element.
Finally it should be noted that：Obviously, above-described embodiment is only intended to clearly illustrate example of the present invention, and simultaneously
The non-restriction to implementation method.For those of ordinary skill in the field, can also do on the basis of the above description
Go out the change or variation of other multi-forms.There is no need and unable to be exhaustive to all of implementation method.And thus drawn
Obvious change that Shen goes out or among changing still in protection scope of the present invention.
Claims (10)
1. a kind of organic solid waste comprehensive treatment equipment, it is characterised in that including multiple storage bins, the first mixer, proportioner,
Fermenting case and screening plant, charging aperture of multiple storage bins respectively with first mixer are connected, and are stored for classifying
Pending waste material, the discharging opening of first mixer is connected with the proportioner, the discharge end of the proportioner and institute
The feed end connection of fermenting case is stated, the discharge end of the fermenting case is connected with the discharge end of the screening plant,
Wherein, the proportioner receives Various Wastes, and the Various Wastes include the waste material from first mixer, institute
State proportioner to receive various waste materials be added in proportion after, be transported to the fermenting case and fermented, complete hair
The waste material of ferment effect is transported to the screening plant carries out screening process.
2. organic solid waste comprehensive treatment equipment according to claim 1, it is characterised in that the fermenting case includes that temperature is mended
Repay system, casing and chain scraper conveyor, the chain scraper conveyor for carrying and conveys fermentation waste in the casing,
Temperature compensation system collection solar energy is simultaneously converted into heat energy point two-way after heat energy and selects at least within all the way to described
Waste material in casing is heated,
Wherein, heat energy is transported to fermentation waste by the first via through the outer wall of the casing, and fermentation waste is heated, the second tunnel
Directly heat energy is conveyed through the mode of air blast to the waste material.
3. organic solid waste comprehensive treatment equipment according to claim 2, it is characterised in that the temperature compensation system includes
Solar heat-collection plate and water tank, the solar heat-collection plate are used to collect solar energy and be converted into heat energy in the water tank
Water is heated, and the hot water circuit in the water tank forms the first temperature control branch road and the second temperature control branch road, and the hot water in the water tank can
Selection flow through the first temperature control branch road and the second branch road at least one,
Wherein, the heat on the first temperature control branch road is used to be delivered in fermentation waste heat energy through the outer wall of the casing,
Heat on the second temperature control branch road is used for the mode through air blast to the logical hot blast of waste material in the casing.
4. organic solid waste comprehensive treatment equipment according to claim 3, it is characterised in that the pipe of the second temperature control branch road
Road is provided with least one heat-sink unit, and the pipeline of the second temperature control branch road passes through the heat-sink unit,
The heat-sink unit includes shell and the radiating fin in the shell, and the shell has first port and second
Port, the first port is connected with the first blower fan, and the second port is used to discharge hot blast.
5. organic solid waste comprehensive treatment equipment according to claim 2, it is characterised in that the chain scraper conveyor each
Carrier bar has ventilated cavity, and first surface and second surface perpendicular to one another respectively, offers on the first surface
Multiple extends to the fresh air inlet of the ventilated cavity, for outside wind to be passed through into the ventilated cavity；
The second surface is provided with multiple ventilation plugs, and is connected with the ventilated cavity, for the closed ventilated cavity, and
Air-flow in the ventilated cavity is released.
6. organic solid waste comprehensive treatment equipment according to claim 5, it is characterised in that the second surface is provided with peace
Dress hole, for installing the ventilation plug；
The outlet air end of the ventilation plug is provided with primary diaphragm, and the primary diaphragm includes multiple diaphragm valves, multiple diaphragm valves
Outward flange be individually fixed in the outlet air end of the ventilation plug, slitless connection between inside edge so that the closed outlet air end,
The air intake of the ventilation plug is provided with secondary diaphragm, multiple current stabilization holes is offered on the secondary diaphragm, for stablizing gas
Stream.
7. organic solid waste comprehensive treatment equipment according to claim 2, it is characterised in that the fermenting case also includes monitoring
System, built with fermentation waste, the monitoring system includes drive device and is fixed in the drive device casing
At least one probe, the drive device is slidably secured on the inwall of the casing, and the drive device is used to drive
The dynamic probe movement, so as to detect the waste material of diverse location in the casing, and drive the probe to move up and down will be described
Probe insertion waste material in or depart from waste material.
8. organic solid waste comprehensive treatment equipment according to claim 1, it is characterised in that the storage bin includes the first storage
Feed bin, the second storage bin, the 3rd storage bin, the 4th storage bin, wherein,
First storage bin is used for temporary livestock waste material of dying of illness, and second storage bin is used to keep in kitchen sorting waste material, institute
State the 3rd storage bin is used to keep in plant's excrement waste material for keeping in municipal sludge waste material, the 4th storage bin.
9. a kind of organic solid waste comprehensive processing technique, it is characterised in that comprise the following steps：
A) livestock waste material, the kitchen of, dying of illness sort waste material, municipal sludge waste material and plant's excrement and carry out waste material and be delivered to respectively
First mixer is mixed, and forms mixing waste；
B) mixing waste, is delivered to proportioner, and through the proportioner by the mixing waste, auxiliary material and return
Material is added in proportion, forms proportioning waste material；
C) the proportioning waste material, is delivered into fermenting case to be fermented, screening plant is delivered to after the completion of fermentation and is sieved；
D), remaining waste material continues to return to the proportioner on the screening plant, is processed again.
10. organic solid waste comprehensive processing technique according to claim 9, it is characterised in that the proportioning waste material is described
High temperature fermentation stage, mesophilic digestion stage and cold fermentation stage are sequentially passed through in fermenting case, wherein,
In the high temperature fermentation stage, when the temperature in fermentation waste is more than preset temperature, the release of start-up temperature compensation system
Cold wind, and waste material is stirred.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710210098.7A CN106862246B (en) | 2017-03-31 | 2017-03-31 | Organic solid waste comprehensive treatment equipment and technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710210098.7A CN106862246B (en) | 2017-03-31 | 2017-03-31 | Organic solid waste comprehensive treatment equipment and technique |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106862246A true CN106862246A (en) | 2017-06-20 |
| CN106862246B CN106862246B (en) | 2019-09-10 |
Family
ID=59159730
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710210098.7A Expired - Fee Related CN106862246B (en) | 2017-03-31 | 2017-03-31 | Organic solid waste comprehensive treatment equipment and technique |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106862246B (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107216170A (en) * | 2017-07-18 | 2017-09-29 | 张志军 | Organic solid waste fermentation is with chain board component and applies its chain scraper conveyor |
| CN107227255A (en) * | 2017-07-18 | 2017-10-03 | 张志军 | Organic solid waste fermenting case |
| CN107235755A (en) * | 2017-07-18 | 2017-10-10 | 张志军 | Organic solid waste fermenting case |
| CN107324857A (en) * | 2017-07-18 | 2017-11-07 | 张志军 | Organic solid waste fermentation is with chain board component and applies its chain scraper conveyor |
| CN107382399A (en) * | 2017-07-18 | 2017-11-24 | 张志军 | Organic solid waste fermenting case |
| CN108503397A (en) * | 2018-05-21 | 2018-09-07 | 浙江工业大学 | A kind of domestic type kitchen garbage treater and Food waste treatment method |
| CN112662549A (en) * | 2021-01-19 | 2021-04-16 | 济宁职业技术学院 | Accurate control system of garbage bin pre-fermentation temperature |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102020494A (en) * | 2009-09-22 | 2011-04-20 | 四平市立山机械制造有限责任公司 | Process and equipment for making organic composite fertilizer from sludge and straw |
| CN202898246U (en) * | 2012-08-23 | 2013-04-24 | 北京机电院高技术股份有限公司 | Integrated system for biological treatment of urban garden green waste |
| CN203333509U (en) * | 2012-04-18 | 2013-12-11 | 武汉日清生物科技有限公司 | Quick heating device for fermentation of high temperature aerobic composting |
| KR20130139568A (en) * | 2012-06-13 | 2013-12-23 | 주식회사 지성이엔지 | Environmentally friendly waste disposal system |
| CN203907732U (en) * | 2014-04-24 | 2014-10-29 | 杭州永仁建设有限公司 | Economic building heating and ventilation system |
| CN104928098A (en) * | 2015-05-13 | 2015-09-23 | 贵州珍酒酿酒有限公司 | Vinasse crushing and airing machine |
| CN205590584U (en) * | 2016-03-31 | 2016-09-21 | 登封快丰收农业发展有限公司 | Bio - organic fertilizer production line |
-
2017
- 2017-03-31 CN CN201710210098.7A patent/CN106862246B/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102020494A (en) * | 2009-09-22 | 2011-04-20 | 四平市立山机械制造有限责任公司 | Process and equipment for making organic composite fertilizer from sludge and straw |
| CN203333509U (en) * | 2012-04-18 | 2013-12-11 | 武汉日清生物科技有限公司 | Quick heating device for fermentation of high temperature aerobic composting |
| KR20130139568A (en) * | 2012-06-13 | 2013-12-23 | 주식회사 지성이엔지 | Environmentally friendly waste disposal system |
| CN202898246U (en) * | 2012-08-23 | 2013-04-24 | 北京机电院高技术股份有限公司 | Integrated system for biological treatment of urban garden green waste |
| CN203907732U (en) * | 2014-04-24 | 2014-10-29 | 杭州永仁建设有限公司 | Economic building heating and ventilation system |
| CN104928098A (en) * | 2015-05-13 | 2015-09-23 | 贵州珍酒酿酒有限公司 | Vinasse crushing and airing machine |
| CN205590584U (en) * | 2016-03-31 | 2016-09-21 | 登封快丰收农业发展有限公司 | Bio - organic fertilizer production line |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107216170A (en) * | 2017-07-18 | 2017-09-29 | 张志军 | Organic solid waste fermentation is with chain board component and applies its chain scraper conveyor |
| CN107227255A (en) * | 2017-07-18 | 2017-10-03 | 张志军 | Organic solid waste fermenting case |
| CN107235755A (en) * | 2017-07-18 | 2017-10-10 | 张志军 | Organic solid waste fermenting case |
| CN107324857A (en) * | 2017-07-18 | 2017-11-07 | 张志军 | Organic solid waste fermentation is with chain board component and applies its chain scraper conveyor |
| CN107382399A (en) * | 2017-07-18 | 2017-11-24 | 张志军 | Organic solid waste fermenting case |
| CN107216170B (en) * | 2017-07-18 | 2018-06-01 | 上海东振环保工程技术有限公司 | Organic solid waste fermentation is with carrier bar component and applies its chain scraper conveyor |
| CN107227255B (en) * | 2017-07-18 | 2018-07-24 | 安徽安成工业设备有限公司 | Organic solid waste fermenting case |
| CN108503397A (en) * | 2018-05-21 | 2018-09-07 | 浙江工业大学 | A kind of domestic type kitchen garbage treater and Food waste treatment method |
| CN112662549A (en) * | 2021-01-19 | 2021-04-16 | 济宁职业技术学院 | Accurate control system of garbage bin pre-fermentation temperature |
| CN112662549B (en) * | 2021-01-19 | 2022-12-16 | 深圳市艾瑞德控制技术有限公司 | Accurate control system of garbage bin pre-fermentation temperature |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106862246B (en) | 2019-09-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106862246B (en) | Organic solid waste comprehensive treatment equipment and technique | |
| RU69858U1 (en) | INSTALLATION OF BIOCOMPOSITION, MATRUSION AND DRYING OF WATER-FREE WASTE WATER SEDIMENTS | |
| CN206751692U (en) | Organic fertilizer Rapid Fermentation system | |
| CN106396769A (en) | Process equipment for composting and rapid aerobic fermentation of sludge, and automatic control scheme for composting and rapid aerobic fermentation process | |
| CN108623348A (en) | Biological organic fertilizer production system | |
| CN104690073B (en) | A kind of biological dewatered method of garage type | |
| CN107282601B (en) | Buried house refuse is reduced resource integrated device and its processing method | |
| US5451523A (en) | Apparatus for composting organic waste material | |
| CN106431540A (en) | Intelligent control method and system for microbial decomposition process of organic matters | |
| Sesay et al. | Aerated static pile composting of municipal solid waste (MSW): A comparsion of positive pressure aeration with hybrid positive and negative aeration | |
| CN111530899B (en) | Integrated multifunctional household garbage treatment equipment | |
| CN206925140U (en) | A kind of buried house refuse is reduced resource integrated device | |
| CN112830834B (en) | Aerobic fermentation treatment system | |
| CN103265343A (en) | Method for treating domestic garbage by utilizing biotechnology | |
| CN110759767A (en) | Kitchen waste stirred tank reactor | |
| CN108503398A (en) | The aerobic fermentation equipment of fully-automatic sealing enclosed environmental sanitation rubbish | |
| CN206127311U (en) | Solid high -ternperature aerobic zymolysis reaction system | |
| CN207086545U (en) | A kind of house refuse is reduced recycling buried type integrated device | |
| CN111018582A (en) | Organic waste biological fermentation reaction equipment and organic fertilizer production line | |
| JP2519623B2 (en) | Fertilizer manufacturing method | |
| CN203174000U (en) | Sludge biological drying and aeration system with air-blasting lower part and air-exhausting upper part | |
| CN206418047U (en) | A kind of automatic control equipment of utilization afforestation castoff compost organic and inorganic fertilizer | |
| JP2001510139A5 (en) | ||
| CN107377580A (en) | House refuse is reduced method of resource and buried type integrated device | |
| AU2009202521A1 (en) | Improvements to composting systems |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190910 |