CN106694524A - Garbage on-site in-situ resource treatment system and method - Google Patents
Garbage on-site in-situ resource treatment system and method Download PDFInfo
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- CN106694524A CN106694524A CN201710042691.5A CN201710042691A CN106694524A CN 106694524 A CN106694524 A CN 106694524A CN 201710042691 A CN201710042691 A CN 201710042691A CN 106694524 A CN106694524 A CN 106694524A
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- machine
- heat exchanger
- fermentation machine
- liquid
- solid
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- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims abstract description 23
- 238000011065 in-situ storage Methods 0.000 title claims abstract description 9
- 238000000855 fermentation Methods 0.000 claims abstract description 58
- 230000004151 fermentation Effects 0.000 claims abstract description 58
- 239000007788 liquid Substances 0.000 claims abstract description 54
- 238000010563 solid-state fermentation Methods 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 230000007246 mechanism Effects 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 claims description 20
- 239000011230 binding agent Substances 0.000 claims description 14
- 239000007787 solid Substances 0.000 claims description 12
- 239000002068 microbial inoculum Substances 0.000 claims description 10
- 238000003672 processing method Methods 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 8
- 238000004064 recycling Methods 0.000 claims description 6
- 238000010564 aerobic fermentation Methods 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims description 3
- 238000000926 separation method Methods 0.000 abstract description 7
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 235000013410 fast food Nutrition 0.000 abstract description 2
- 230000009286 beneficial effect Effects 0.000 abstract 1
- 238000004134 energy conservation Methods 0.000 abstract 1
- 238000001125 extrusion Methods 0.000 description 10
- 238000007599 discharging Methods 0.000 description 9
- 244000005700 microbiome Species 0.000 description 5
- 210000000988 bone and bone Anatomy 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000003895 organic fertilizer Substances 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000010806 kitchen waste Substances 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 235000011837 pasties Nutrition 0.000 description 2
- 238000010791 quenching Methods 0.000 description 2
- 230000000171 quenching effect Effects 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000256113 Culicidae Species 0.000 description 1
- 241000255925 Diptera Species 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 238000005276 aerator Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 238000003698 laser cutting Methods 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 235000008935 nutritious Nutrition 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 239000002351 wastewater Substances 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
The invention belongs to the field of garbage treatment and particularly relates to a garbage on-site in-situ resource treatment system and method. The system sequentially comprises a feeding port, a three-axis breaking machine, a primary fermentation machine, a solid-liquid separation machine, an oil-water separator and a liquid-state fermentation machine from the starting end. The solid-liquid separation machine is further connected with a solid-state fermentation machine. The primary fermentation machine and the liquid-state fermentation machine conduct heat exchange treatment through a heat exchanger. The system and method are suitable for garbage on-site treatment of mechanisms such as canteens of offices and schools and fast food restaurants, have the beneficial effects that the occupied area is small, energy consumption is low, noise is low, the cost is low, economic benefits are high, and no secondary pollution exists, conform to the ideas of environment friendliness, low consumption, energy conservation and emission reduction and have great market prospects and economic value.
Description
Technical field
The invention belongs to field of garbage disposal, and in particular to a kind of rubbish in-situ recycling treatment system and its treatment
Method.
Background technology
Kitchen garbage have high-moisture percentage, high organic content, it is perishable, nutritious the features such as, kitchen garbage is being deposited
Put, collect, transporting and disposal process in, because its moisture content and content of organics are higher, easily in the short period of time rot hair
Smelly and growth mosquitos and flies, pollutes urban environment, how efficiently and rapidly to dispose rubbish from cooking, is always the universal concern of government and society
Problem.The current processing mode of kitchen garbage that dining room restaurant produces has several:Kitchen garbage is put into dustbin, is given specially
Industry treatment company is focused on;Kitchen garbage is crushed, sewer is entered;Kitchen garbage is carried out into separation of solid and liquid,
Moisture is entered into sewer, solid fermentation produces organic fertilizer;Kitchen garbage is put into biochemical reactor, carbon dioxide is reacted into
Environment is entered with water;Any of the above processing method all generally faces:Kitchen garbage treatment thoroughly, stench is not produced easily, to water
Polluted with air.Treatment high energy consumption, big, the of poor benefits problem of investment.
Therefore finding a kind for the treatment of kitchen garbage technology and equipment efficiently, quick, economic turns into the urgent of existing market
Need.
The content of the invention
Therefore, the technical problems to be solved by the invention are the technical bottleneck for overcoming prior art, so as to propose one kind
Rubbish in-situ recycling processing method and equipment.
In order to solve the above technical problems, the invention discloses a kind of rubbish in-situ recycling treatment system, the system
System sequentially includes since start end:Dog-house, three axle disintegrating machines, primary fermentation machine, solid-liquid separating machine, oil water separator, liquid
State fermentation machine;
The solid-liquid separating machine is also associated with a solid state fermentation machine;
The primary fermentation machine, liquid state fermentation machine carry out heat exchange process by heat exchanger.
Preferably, the primary fermentation machine, liquid state fermentation machine, solid state fermentation machine are provided with microbial inoculum addition tank, the place
Reason system is also associated with underflow conveying mechanism.
Preferably, the three axles disintegrating machine includes frame, be provided with the frame the first broken shaft for being parallel to each other and
Second broken shaft, the first broken shaft top is provided with the binder axle parallel with first broken shaft, and described first crushes
Axle can be relatively rotated with second broken shaft, and first broken shaft can drive the binder axle to rotate, and described first crushes
Axle surface is provided with the first extruding tooth, and the second broken shaft surface is provided with second set with the described first extruding space of teeth
Extruding tooth, the binder axle surface is provided with the 3rd extruding tooth being correspondingly arranged with the described first extruding tooth.
Preferably, the solid-liquid separating machine includes:Sleeve, outer barrel with sieve aperture, varying pitch screw;
The sleeve with sieve aperture is set in outside the varying pitch screw;
The outer barrel is provided with outside the sleeve with sieve aperture.
Preferably, the heat exchanger includes:Core, heat exchanger, heat exchanger shell and electromagnetic heating coil, the heat
Exchanger core includes some heat-exchange tubes and heat-exchange tube installing plate, and the heat-exchange tube is installed on two pieces of heat-exchange tube installing plates
Between, it is parallel to each other between heat-exchange tube;The heat exchanger shell is surrounded on the core, heat exchanger, is connected on heat exchanger
Accommodating heat conduction is formed with the middle of the heat-exchange tube installing plate at core two ends, the heat exchanger shell and the heat-exchange tube installing plate
The cavity of medium;The electromagnetic heating coil is socketed on the heat exchanger shell;The heat exchange at the core, heat exchanger two ends
Pipe installing plate is respectively connected to gas pipeline interface;The heat exchanger shell it is relative be respectively provided on two sides with fluid pipeline interface.
The invention also discloses the method that system described in any one is used for garbage disposal, methods described is:
Rubbish is put into dog-house, break process is carried out hence into three axle disintegrating machines, the material after crushing enters addition
Microorganism be combined decompose microbial inoculum primary fermentation machine fermented;
The material that will be fermented carries out separating treatment through solid-liquid separator;
The solid that separating treatment goes out is put into solid state fermentation machine carries out aerobic fermentation;
The liquid that separating treatment goes out is put into oil water separator carries out separating treatment, and the liquid isolated is sent out into liquid
Ferment machine is fermented.
Preferably, the fermentation temperature of the primary fermentation machine is 28 DEG C -35 DEG C;Fermentation time is 8-24 hours.
Preferably, the fermentation temperature of the solid state fermentation machine is 28 DEG C -35 DEG C, and fermentation time is 8-24 hours.
Preferably, the fermentation temperature of the liquid state fermentation machine is 28 DEG C -35 DEG C, and fermentation time is 8-24 hours.
Above-mentioned technical proposal of the invention has advantages below compared to existing technology:System and method of the present invention are adapted to
The rubbish treatment in situ of the mechanisms such as office, the dining room of school and fast food restaurant, few with floor space, energy consumption is low, low noise, cost
Lowly, high financial profit, the advantages of do not have secondary pollution, meets environmental protection and low consumption theory;With great market prospects and warp
Ji value.
Brief description of the drawings
In order that present disclosure is more likely to be clearly understood, below according to specific embodiment of the invention and combine
Accompanying drawing, the present invention is further detailed explanation, wherein
Fig. 1 is the schematic diagram of system described in embodiment;
Fig. 2 is the structural representation of system described in embodiment;
Fig. 3 is the structural representation of system described in embodiment;
Fig. 4 is the structural representation of system described in embodiment;
Fig. 5 is the structural representation of system described in embodiment
Fig. 6 is the structural representation of system described in embodiment;
Fig. 7 is the structural representation of system described in embodiment;
Fig. 8 is the structural representation of system described in embodiment.
Specific embodiment
Embodiment 1 is present embodiment discloses a kind of rubbish in-situ recycling treatment system (as described in Figure 1), the system
System sequentially includes since start end:Dog-house, three axle disintegrating machines, solid-liquid separating machine, primary fermentation machine;
The solid-liquid separating machine is connected with a solid state fermentation machine and an oil water separator;
The oil water separator is connected with a liquid state fermentation machine;
The primary fermentation machine, liquid state fermentation machine, solid state fermentation machine are respectively connected with a heat exchanger.
Preferably, the primary fermentation machine, liquid state fermentation machine, solid state fermentation machine are respectively connected with microbial inoculum addition tank, the place
Reason system is also associated with underflow conveying mechanism.
Preferably, the primary fermentation machine, liquid state fermentation machine, solid state fermentation machine are respectively connected with microbial inoculum addition tank, the place
Reason system is also associated with automatic controls.
Wherein, as in Figure 2-4, the three axles disintegrating machine includes:Frame 1, the top of the frame 1 be provided with feeding mouth 2,
Bottom is provided with discharging opening 3, inside the input frame 1 of kitchen waste feeding mouth 2, by being discharged by discharging opening 3 after break process.
The frame 1 is internally provided with the first broken shaft 4 and the second broken shaft 5 being parallel to each other, and described first crushes
The top of axle 4 is provided with the binder axle 6 parallel with first broken shaft 4, and the material of first broken shaft 4 is hexagonal steel, institute
Stating the first broken shaft 4 can relatively rotate with second broken shaft 5, and first broken shaft 4 can drive 6 turns of the binder axle
Dynamic, the surface of the first broken shaft 4 is provided with the first extruding tooth 7, and the surface of the second broken shaft 5 is provided with to be squeezed with described first
Knob 7 spaced second extrudes tooth 8, and the surface of binder axle 6 is provided with the be correspondingly arranged with the described first extruding tooth 7
Three extruding teeth 9.Wherein, the material of the first extruding extruding extruding tooth 9 of tooth the 8, the 3rd of tooth 7, second is 40Cr steel, and thickness is 10mm,
Its hardness is up to 301-340HB, and quenching degree is higher than 45 steel, the Surface hardening treatment such as suitable high-frequency quenching, flame hardening, and the
The sectional view of the one extruding extruding extruding tooth 9 of tooth the 8, the 3rd of tooth 7, second is isosceles trapezoid, and the corner angle of isosceles trapezoid is
100°.
Further, be arranged with the first extruding wheel 10 outside first broken shaft 4, first extruding wheel 10 with it is described
The position of the first extruding tooth 7 is corresponded and sets, and the first extruding tooth 7 is corresponded and is arranged at outside first extruding wheel 10
Portion;The second extruding wheel 11, second extruding wheel 11 and the described second extruding tooth 8 one are arranged with outside second extrusion axis 5
One is correspondingly arranged, and the second extruding tooth 8 is corresponded and is arranged at outside second extruding wheel 11;Outside the binder axle 6
The 3rd extruding wheel 12 is provided with, the 3rd extruding wheel 12 is corresponded with the described 3rd extruding tooth 9 and set, the 3rd extruding
Tooth 9 is corresponded and is arranged at outside the 3rd extruding wheel 12, the first extruding wheel 10, the second extruding wheel 11, the 3rd extruding wheel 12
Thickness be 10mm.
In order to realize transmission, one end of first broken shaft 4 is connected with first gear 13, second broken shaft 5 with
The identical one end of the first gear 13 be connected with the intermeshing second gear 14 of the first gear 13, described first break
Broken axle 4 is rotated and drives first gear 13 to rotate, and first gear 13 drives second gear 14 to rotate so as to drive described second to crush
Axle 5 is relatively rotated with first broken shaft 4;The binder axle 6 is connected with the 3rd with the identical one end of the first gear 13
Gear 15, the 3rd gear 15 is connected by travelling gear 16 with the first gear 13, the travelling gear 16 simultaneously with
The gear 15 of the first gear 13 and the 3rd is engaged, and first broken shaft 4 is rotated and drives first gear 13 to rotate, first gear
13 band nutating gears 16 are rotated, and travelling gear 16 and then drive the 3rd gear 15 to rotate, final to drive binder axle 16 to rotate, and are entered
During material, the first broken shaft 4 drives binder axle 6 to rotate down, by kitchen garbage introduce the first broken shaft 4 and the second broken shaft 5 it
Between.
Also include the drive mechanism for driving first broken shaft 4 to rotate, the drive mechanism is conventional motor,
The motor is arranged at the one end away from the first gear 13.
The kitchen garbage breaking system work process is as follows:
Kitchen garbage input in bulk or band bag are put into the frame 1, the bone in kitchen garbage, wooden chopsticks plastics
Bag etc. need not specially be chosen, can break process together, fermented treatment can very easily screen out after drying and.
After material enters frame 1, binder axle 6 is rotated down, and the kitchen garbages such as bone is smoothly entered the He of the first broken shaft 4
Between second broken shaft 5, two extruding wheels and extruding tooth outside the first broken shaft 4, the second broken shaft 5 are relatively rotated, extruding
Kitchen garbage material, reaches bone and crushes, and the effect that polybag will not be rubbed.After this crushing system of kitchen waste is broken,
Rice, steamed bun meat etc. are broken into pasty state;Bone is broken into bulk;Vegetables etc. are broken into pasty state, and crude fibre is broken into short strip shape;
Wooden chopsticks are broken into chopped fiber shape;Polybag is broken into strip and block.When crushing system runs into hard thing and do not crush, by torque sensing
Device and automatically control, broken shaft can be controlled to rotate backward, normal rotation is then recovered again, after the completion of crushing system work, beat
Wash-out valve is opened, the inside of frame 1 is sprayed clean.
Wherein, as shown in figure 5, the solid-liquid separation system includes:Adjustable pressure plate 208, charging aperture 207, discharging opening
201st, the sleeve 206 with sieve aperture, main shaft 205, outer barrel 202, delivery port 204, extrusion spiral 203;
The adjustable pressure plate 208 is arranged on the top of the system, can be to the extrusion gap of the extrusion spiral 203
It is adjusted;A main shaft 205 through the system is provided with the system;The extrusion spiral 203 is around the master
The spiral of axle 205 is set;The varying pitch of the extrusion spiral 203 is 200-50MM;
The delivery port 204 is arranged on the lower section of the system, for rubbish to be extruded after waste water discharge;
The sleeve 206 with sieve aperture is provided with outside the extrusion spiral 203;Outside the sleeve 206 with sieve aperture
It is the outer barrel 202;The charging aperture 201, discharging opening 207 are arranged on the outer barrel 202;
The system is additionally provided with a motor reductor;
The adjustable stripper plate 208 can adjust discharge state, control the change of moisture content.
The difference of this equipment and general solid-liquid separating machine filter screen:It is that general filter screen uses circular hole, and the size of circular hole and plate
Thick relevant, slab intensity is high, but can not go out aperture, so general solid-liquid separating machine, particles in liquid is a lot.This filter screen by
Laser cutting is formed, and very narrow gap can be cut out on slab, reaches the effect of effective separation of solid and liquid, and equipment keeps
Good mechanical strength.
This equipment gap opening selects 30 degree of inclinations angle, makes to reduce resistance during screw propulsion, and can effectively cut fibre
Dimension class material.
This equipment uses y-type structure, and moisture can be made quickly to exclude, and reduces the moisture content of solid content.
This equipment is made up of several functional parts, with plurality of specifications, can conveniently constitute, and adapts to different treating capacities.
The equipment operation principle:Before material access arrangement, it is first powered on, extrusion spiral is rotated;Material is entered by charging aperture;
Material is moved under extrusion spiral drive to discharging opening direction;Moisture in material flows out through the gap of filter screen, through going out liquid material
Mouth discharge;The distance between stripper plate and discharging opening of discharging opening are adjusted, the solid aqueous rate of discharging is reached requirement;Solids
From the discharge of solids discharging opening;Extrusion spiral is driven by speed-variable speed reducer;Speed-variable speed reducer has overload protection, and positive and negative
Rotating function, can keep equipment to run well.The difference of this equipment and general solid-liquid separating machine filter screen:It is that general filter screen uses circle
Hole, and the size of circular hole is relevant with thickness of slab, slab intensity is high, but can not go out aperture, so general solid-liquid separating machine, in liquid
Particulate matter is a lot.This filter screen is formed by being cut by laser, and very narrow gap can be cut out on slab, reaches effective separation of solid and liquid
Effect, and equipment keeps good mechanical strength.
Wherein, Fig. 6 to Fig. 8, the heat exchanger, including core, heat exchanger 307, the and of heat exchanger shell 301 are referred to
Electromagnetic heating coil 302, the core, heat exchanger 307 includes two pieces of heat-exchange tube installing plates 304 and some heat-exchange tubes 303,
It is parallel to each other between heat-exchange tube 303, the two ends of heat-exchange tube 303 are respectively connected to one piece of heat-exchange tube installing plate 304;
The heat exchanger shell 301 is surrounded on the core, heat exchanger 307, is connected on the two ends of core, heat exchanger 307
Heat-exchange tube installing plate 304, accommodating leading is formed with the middle of the heat exchanger shell 301 and the heat-exchange tube installing plate 304
The cavity of thermal medium;
The electromagnetic heating coil 302 is socketed on the heat exchanger shell 301;
The heat-exchange tube installing plate 304 at the two ends of the core, heat exchanger 307 is respectively connected to gas pipeline interface 306;
The heat exchanger shell 301 it is relative be respectively provided on two sides with fluid pipeline interface 305.
The equipment principle is as follows:By setting electromagnetic heating coil on the heat exchanger, it is easy to for heat exchanger is provided
Control temperature and heating efficiency pyrotoxin high, realize the precision control to microbial fermentation environment temperature.
The present embodiment also discloses system described in embodiment 1 for the method for garbage disposal, and methods described is:
Rubbish is put into dog-house, break process is carried out hence into three axle disintegrating machines, the material after crushing enters addition
Microorganism be combined decompose microbial inoculum primary fermentation machine fermented;
The material that will be fermented carries out separating treatment through solid-liquid separator;
The solid that separating treatment goes out is put into solid state fermentation machine carries out aerobic fermentation;
The liquid that separating treatment goes out is put into oil water separator carries out separating treatment, and the liquid isolated is sent out into liquid
Ferment machine is fermented.
Preferably, the fermentation temperature of the primary fermentation machine is 28 DEG C -35 DEG C;Fermentation time is 8-24 hours.
Preferably, the fermentation temperature of the solid state fermentation machine is 28 DEG C -35 DEG C, and fermentation time is 8-24 hours.
Preferably, the fermentation temperature of the liquid state fermentation machine is 28 DEG C -35 DEG C, and fermentation time is 8-24 hours.
The agricultural microbial inoculum of multifunctional composite microbe is added in liquid state fermentation.
It is solid-state microorganism organic fertilizer after the product of solid state fermentation is through the screening in 2mm apertures.
The product of liquid state fermentation is liquid microbial organic fertilizer.
Special bacteria is all added in solid state fermentation and liquid state fermentation, can effectively solve the problems, such as kitchen garbage treatment salinity and
Foul smell problem.
Control system is made up of PLC and touch-screen and configuration software and multiple sensors;Full-automatic operation is realized, remotely
Monitoring.
The operation principle of whole system:Rubbish is put into dog-house, dog-house is provided with proximity transducer, and control is slidingly sealed
The open and close of lid;Material Sensor controls the start and stop of disintegrating machine;Material after broken enters primary fermentation machine;Treat material
After dispensing is finished, program starts fermentation machine agitator;The compound microbial inoculum that decomposes of microorganism is added in proportion automatically;Heat exchanger works
Fermentation machine initial heat is provided;Aerator provides air needed for aerobic fermentation;The material for fermenting is separated through solid-liquid separator;Point
The solid for separating out ferments into solid-state fermenter;Solid state fermentation is using aerobic+simultaneous oxygen technique;Solid state fermentation addition is multi-functional compound
The agricultural microbial inoculum of microorganism;Oil water separator is initially entered through the liquid of solid-liquid separation.The grease isolated through oil water separator
Into oil storage tank.The liquid separated through oil water separator ferments into liquid fermentation fermentor.
Obviously, above-described embodiment is only intended to clearly illustrate example, and not to the restriction of implementation method.It is right
For those of ordinary skill in the art, can also make on the basis of the above description other multi-forms change or
Change.There is no need and unable to be exhaustive to all of implementation method.And the obvious change thus extended out or
Among changing still in the protection domain of the invention.
Claims (9)
1. a kind of rubbish in-situ recycling treatment system, it is characterised in that the system sequentially includes since start end:
Dog-house, three axle disintegrating machines, primary fermentation machine, solid-liquid separating machine, oil water separator, liquid state fermentation machine;
The solid-liquid separating machine is also associated with a solid state fermentation machine;
The primary fermentation machine, liquid state fermentation machine carry out heat exchange process by heat exchanger.
2. the system as claimed in claim 1, it is characterised in that the primary fermentation machine, liquid state fermentation machine, solid state fermentation machine are equal
Microbial inoculum addition tank is provided with, the processing system is also associated with underflow conveying mechanism.
3. the system as described in any one of claim 1 or 2, it is characterised in that the three axles disintegrating machine includes frame, the machine
The first broken shaft and the second broken shaft being parallel to each other are provided with frame, the first broken shaft top is provided with and described first
The parallel binder axle of broken shaft, first broken shaft can be relatively rotated with second broken shaft, and first broken shaft can
The binder axle is driven to rotate, the first broken shaft surface is provided with the first extruding tooth, the second broken shaft surface is set
There is the second extruding tooth set with the described first extruding space of teeth, the binder axle surface is provided with and the described first extruding tooth pair
The 3rd extruding tooth that should be set.
4. system as claimed in claim 3, it is characterised in that the solid-liquid separating machine includes:It is sleeve with sieve aperture, outer
Cylinder, varying pitch screw;
The sleeve with sieve aperture is set in outside the varying pitch screw;
The outer barrel is provided with outside the sleeve with sieve aperture.
5. system as claimed in claim 4, it is characterised in that the heat exchanger includes:Core, heat exchanger, shell heat exchanger
Body and electromagnetic heating coil, the core, heat exchanger include some heat-exchange tubes and heat-exchange tube installing plate, the heat-exchange tube
It is installed between two pieces of heat-exchange tube installing plates, is parallel to each other between heat-exchange tube;The heat exchanger shell is surrounded on described
Core, heat exchanger, is connected on the heat-exchange tube installing plate at core, heat exchanger two ends, the heat exchanger shell and the heat exchange
The cavity of accommodating heat conduction medium is formed with the middle of pipe installing plate;The electromagnetic heating coil is socketed on the heat exchanger shell;
The heat-exchange tube installing plate at the core, heat exchanger two ends is respectively connected to gas pipeline interface;The heat exchanger shell it is relative two
Side is respectively equipped with fluid pipeline interface.
6. the method that the system as described in claim any one of 1-5 is used for garbage disposal, it is characterised in that methods described is:
Rubbish is put into dog-house, break process is carried out hence into three axle disintegrating machines, the material after crushing enters the micro- of addition
The compound primary fermentation machine for decomposing microbial inoculum of biology is fermented;
The material that will be fermented carries out separating treatment through solid-liquid separator;
The solid that separating treatment goes out is put into solid state fermentation machine carries out aerobic fermentation;
The liquid that separating treatment goes out is put into oil water separator carries out separating treatment, and the liquid isolated enters liquid state fermentation machine
Fermented.
7. processing method as claimed in claim 6, it is characterised in that in the processing method, the hair of the primary fermentation machine
Ferment temperature is 28 DEG C -35 DEG C;Fermentation time is 8-24 hours.
8. processing method as claimed in claim 7, it is characterised in that in the processing method, the hair of the solid state fermentation machine
Ferment temperature is 28 DEG C -35 DEG C, and fermentation time is 8-24 hours.
9. processing method as claimed in claim 8, it is characterised in that in the processing method, the hair of the liquid state fermentation machine
Ferment temperature is 28 DEG C -35 DEG C, and fermentation time is 8-24 hours.
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CN201710042691.5A CN106694524A (en) | 2017-01-20 | 2017-01-20 | Garbage on-site in-situ resource treatment system and method |
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CN201710042691.5A CN106694524A (en) | 2017-01-20 | 2017-01-20 | Garbage on-site in-situ resource treatment system and method |
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