CN207471540U - Kitchen castoff and consumer waste incineration coprocessing system - Google Patents
Kitchen castoff and consumer waste incineration coprocessing system Download PDFInfo
- Publication number
- CN207471540U CN207471540U CN201721616185.4U CN201721616185U CN207471540U CN 207471540 U CN207471540 U CN 207471540U CN 201721616185 U CN201721616185 U CN 201721616185U CN 207471540 U CN207471540 U CN 207471540U
- Authority
- CN
- China
- Prior art keywords
- kitchen castoff
- coprocessing
- filter
- collecting tank
- waste incineration
- 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.)
- Active
Links
- 238000004056 waste incineration Methods 0.000 title claims abstract description 26
- 239000002699 waste material Substances 0.000 claims abstract description 39
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 33
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 29
- 239000000706 filtrate Substances 0.000 claims abstract description 25
- 238000001914 filtration Methods 0.000 claims abstract description 6
- 238000006297 dehydration reaction Methods 0.000 claims description 25
- 238000002485 combustion reaction Methods 0.000 claims description 9
- 239000002893 slag Substances 0.000 claims description 6
- 208000005156 Dehydration Diseases 0.000 description 21
- 239000007788 liquid Substances 0.000 description 15
- 239000000126 substance Substances 0.000 description 5
- 238000000855 fermentation Methods 0.000 description 4
- 230000004151 fermentation Effects 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 230000035943 smell Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000001764 infiltration Methods 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 238000011026 diafiltration Methods 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 210000000988 Bone and Bones Anatomy 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000005039 chemical industry Methods 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 239000010806 kitchen waste Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000813 microbial Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 230000001954 sterilising Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Abstract
The utility model discloses kitchen castoffs and consumer waste incineration coprocessing system, it includes kitchen castoff collecting tank (1), and kitchen castoff collecting tank (1) is connected with scalping (2), pulverizer (5), desander (6) and biogas generating device (7) in turn through pipeline；Collecting methane tank (9) and centrifugal dehydrator (11) are connected on biogas generating device (7)；Centrifugal dehydrator (11) is connected with waste incinerator (14) by conveyer belt (12), and filtrate collecting tank (15) is connected with by drainpipe (13)；Filtrate collecting tank (15) is connected with draining pump (19), filter (18) and atomizer (20) in turn by pipeline.The utility model can not only improve garbage utilization rate, also have the advantages that treatment effeciency is high, cost is relatively low, easy to operate, service life of equipment is long, filtration efficiency is high and percolate treatment effeciency is high.
Description
Technical field
The utility model is related to a kind of garbage reclamation processing system, particularly kitchen castoff is cooperateed with consumer waste incineration
Processing system.
Background technology
At present, some common garbage reclamation processing systems, when handling kitchen garbage, it will usually recycle kitchen castoff
In grease make chemical industry oil, and filled after carrying out sterilization processing to the surplus materials in kitchen castoff so that it is many
Organic substance is wasted, and causes kitchen garbage utilization rate relatively low；When handling house refuse, its percolate can be carried out at biochemistry
Reason, makes percolate reach wastewater discharge standard, such processing mode since biochemical action is slower, causes treatment effeciency relatively low；It needs
When handling a large amount of percolates, larger biochemistry pool is needed, cost is higher；Processing of the bioanalysis to the impurity in percolate simultaneously
Not exclusively so that percolate utilization rate is relatively low；And biochemical treatment percolate needs stringent control percolate temperature and PH, operation
It is cumbersome.Therefore, there is garbage utilization rate is relatively low, treatment effeciency is relatively low, cost is higher and behaviour for existing garbage retrieving system
Make the problem of cumbersome.
Utility model content
The purpose of the utility model is to provide a kind of kitchen castoffs and consumer waste incineration coprocessing system.This
Utility model can not only improve garbage utilization rate, also have the advantages that treatment effeciency is high, cost is relatively low and easy to operate.
The technical solution of the utility model：Kitchen castoff and consumer waste incineration coprocessing system, give up including kitchen
Gurry collecting tank is connected with scalping on kitchen castoff collecting tank through pipeline；Thick slag pipe and discharge nozzle are connected in scalping, is discharged
Pulverizer is connected on pipe；Desander is connected with by pipeline on pulverizer, biogas is connected with by pipeline on desander
Device；Collecting methane tank is connected with by biogas pipe on biogas generating device, is connected on biogas generating device by residue pipe
Centrifugal dehydrator；The bottom end of centrifugal dehydrator is provided with conveyer belt, and drainpipe is connected on centrifugal dehydrator；One end of conveyer belt
Waste incinerator is provided with, one end of drainpipe is provided with filtrate collecting tank；The side of the waste incinerator is provided with diafiltration
Device, percolating device top are provided with grab bucket, and percolating device is located above filtrate collecting tank；Connected on filtrate collecting tank by pipeline
Filter is connected to, draining pump is connected on pipeline；Atomizer is connected with by pipeline on the filter, filter bottom connects
It is connected to scum pipe.
Aforementioned kitchen castoff is helped with being set in consumer waste incineration coprocessing system, in the waste incinerator
Device is fired, auxiliary combustion equipment is connect with collecting methane tank.
In aforementioned kitchen castoff and consumer waste incineration coprocessing system, between the filter and atomizer
Pipeline on be connected with pressure regulator valve.
In aforementioned kitchen castoff and consumer waste incineration coprocessing system, the percolating device includes dehydration pond,
The side side wall in dehydration pond is inclined to set, and the side of dehydration pond sloped sidewall is connected with continuous filter；It is set in the dehydration pond
There are multiple Shaftless screw conveyors being distributed side by side, one end of each Shaftless screw conveyor is arranged at dehydration bottom of pond end,
The other end of each Shaftless screw conveyor is arranged at the top of continuous filter；The bottom end of the dehydration pond and continuous filter is equipped with
Filter opening.
Aforementioned kitchen castoff is in consumer waste incineration coprocessing system, pumping is provided with above the percolating device
Wind turbine.
Aforementioned kitchen castoff in consumer waste incineration coprocessing system, the aperture of the filter opening for 50~
80mm。
In aforementioned kitchen castoff and consumer waste incineration coprocessing system, the Shaftless screw conveyor and dehydration
The sloped sidewall in pond is parallel.
In aforementioned kitchen castoff and consumer waste incineration coprocessing system, the atomizer is arranged on rubbish and burns
It burns in stove, heat shield is socketed on the outside of atomizer.
Aforementioned kitchen castoff in the filtrate collecting tank in consumer waste incineration coprocessing system, being provided with
Strainer, filter screen are arranged on the bottom end of filtrate collecting tank.
Compared with prior art, the utility model improves existing garbage reclamation processing system, by kitchen castoff and
House refuse collaboration is handled, and by the way that kitchen castoff is gone out for producing biogas after decontamination and crushing, biogas can be used for rubbish
The supply of incinerator fuel gas, has produced the waste water energy of biogas and the percolate of house refuse mixes to merge back into and is sprayed onto waste incineration
In stove, reduce the treating capacity of waste water；Kitchen castoff, which has produced the residue after biogas and also can further burn, provides thermal energy, this makes
The organic matter obtained in kitchen castoff is fully utilized；Burning will be directly used in after consumer waste infiltration, improves house refuse
Treatment effeciency；It returns and is sprayed onto in waste incinerator after leachate purification processing, recycle the organic substance in percolate, improve life
The utilization rate of rubbish living；The equipment for handling house refuse simultaneously is less, and cost is relatively low, and handles the equipment operation letter of house refuse
It is single.In addition, the utility model helps incineration firing with auxiliary combustion equipment, incineration firing efficiency is improved；In atomizer outer sheath
Heat shield is connected to, the heat radiation that atomizer is subject to is reduced, so as to improve the service life of atomizer；By percolating device point
Into dehydration pond and continuous filter, and multiple inclined Shaftless screw conveyors are provided in dehydration pond, improve house refuse
Filtration efficiency；Exhaust fan is provided with above percolating device, the foul smell generated during consumer waste infiltration can be removed, reduce ring
Border is polluted, while foul smell is passed through waste incinerator, some fuel gas generated during consumer waste infiltration is utilized, further
Improve the utilization rate of house refuse；The bottom end of filtrate collecting tank is provided with filter screen, preliminary mistake can be carried out to percolate
Filter, further improves filter effect, accelerates percolate processing speed.Therefore, the utility model can not only improve rubbish
Utilization rate, also with treatment effeciency is high, cost is relatively low, easy to operate, service life of equipment is long, filtration efficiency is high and percolate at
Manage the advantages of efficient.
Description of the drawings
Fig. 1 is the structure diagram of the utility model；
Fig. 2 is the structure diagram of percolating device；
Fig. 3 is the structure diagram for being dehydrated pond.
Label in attached drawing for：1- kitchen castoff collecting tanks, 2- scalpings, the thick slag pipes of 3-, 4- discharge nozzles, 5- pulverizers,
6- desanders, 7- biogas generating devices, 8- biogas pipes, 9- collecting methane tanks, 10- residue pipes, 11- centrifugal dehydrators, 12- transmission
Band, 13- drainpipes, 14- waste incinerators, 15- filtrate collecting tanks, 16- percolating devices, 17- grab buckets, 18- filters, 19- rows
Water pump, 20- atomizers, 21- scum pipes, 22- auxiliary combustion equipments, 23- pressure regulator valves, 24- dehydrations pond, 25- continuous filters, 26- are shaftless
Screw conveyor, 27- exhaust fans, 28- filter openings, 29- heat shields, 30- filter screens.
Specific embodiment
The utility model is further described with reference to the accompanying drawings and examples, but is not intended as to the utility model
The foundation of limitation.
Embodiment.Kitchen castoff and consumer waste incineration coprocessing system, are formed as shown in Figures 1 to 3, including kitchen
Waste gathering slot 1 is connected with scalping 2 on kitchen castoff collecting tank 1 through pipeline；Thick slag pipe 3 and discharging are connected in scalping 2
Pipe 4 is connected with pulverizer 5 on discharge nozzle 4；Desander 6 is connected with by pipeline on pulverizer 5, is connected on desander 6 by pipeline
It is connected to biogas generating device 7；Collecting methane tank 9 is connected with by biogas pipe 8 on biogas generating device 7, on biogas generating device 7
Centrifugal dehydrator 11 is connected with by residue pipe 10；The bottom end of centrifugal dehydrator 11 is provided with conveyer belt 12, centrifugal dehydrator 11
On be connected with drainpipe 13；One end of conveyer belt 12 is provided with waste incinerator 14, and one end of drainpipe 13 is provided with filtrate receipts
Collect slot 15；The side of the waste incinerator 14 is provided with percolating device 16, and 16 top of percolating device is provided with grab bucket 17, is percolated
Device 16 is located at 15 top of filtrate collecting tank；Filter 18 is connected with by pipeline on filtrate collecting tank 15, is connected on pipeline
Draining pump 19；Atomizer 20 is connected with by pipeline on the filter 18,18 bottom of filter is connected with scum pipe 21.
Auxiliary combustion equipment 22 is provided in the waste incinerator 14, auxiliary combustion equipment 22 is connect with collecting methane tank 9；The mistake
Pressure regulator valve 23 is connected on pipeline between filter 18 and atomizer 20；The percolating device 16 includes dehydration pond 24, dehydration
The side side wall in pond 24 is inclined to set, and the side of dehydration 24 sloped sidewall of pond is connected with continuous filter 25；In the dehydration pond 24
Multiple Shaftless screw conveyors 26 being distributed side by side are provided with, one end of each Shaftless screw conveyor 26 is arranged at dehydration pond
24 bottom ends, the other end of each Shaftless screw conveyor 26 are arranged at the top of continuous filter 25；It is described to be dehydrated pond 24 and ooze
The bottom end in filter tank 25 is equipped with filter opening 28；16 top of percolating device is provided with exhaust fan 27；The aperture of the filter opening 28 is
50~80mm；The Shaftless screw conveyor 26 is parallel with the sloped sidewall for being dehydrated pond 24；The atomizer 20 is arranged on rubbish
In rubbish incinerator 14, the outside of atomizer 20 is socketed with heat shield 29；Filter screen 30 is provided in the filtrate collecting tank 15,
Filter screen 30 is arranged on the bottom end of filtrate collecting tank 15.
Operation principle：Kitchen castoff is poured into kitchen castoff collecting tank 1, the pipe of 1 bottom end of kitchen castoff collecting tank
Kitchen castoff is transported in scalping 2 by road, and scalping 2 removes impurity larger in kitchen castoff, and impurity is out of thick slag pipe 3
Discharge, the kitchen castoff for filtering completion are transported to by discharge nozzle 4 in pulverizer 5；Pulverizer 5 will be in kitchen castoff
The larger substance refinement such as bone, the kitchen castoff after refinement are transported to by pipeline in desander 6；Desander 6 will eat
The small grains of sand in the waste of kitchen remove, and purified kitchen castoff is transported to by pipeline in biogas generating device 7；Kitchen
For waste by microbial fermentation in biogas generating device 7, the biogas generated after fermentation is delivered to natural pond by biogas pipe 8 by compression
In gas collecting tank 9, remaining waste liquid is transported to by residue pipe 10 in centrifugal dehydrator 11 after fermentation；Centrifugal dehydrator 11 is logical
It crosses centrifugal force to remove moisture in waste liquid, the waste liquid of discharge is delivered to by drainpipe 13 in filtrate collecting tank 15, dewatered residual
Slag is transmitted band 12 and is delivered in waste incinerator 14 so that kitchen castoff is fully utilized.
House refuse is poured into percolating device 16, house refuse falls into the bottom in dehydration pond 24 due to gravity, together
When house refuse in waste liquid can from dehydration 24 bottom of pond filter opening 28 flow out；It is defeated that multiple shaftless screws are provided in dehydration pond 24
Machine 26 is sent, all Shaftless screw conveyors 26 arrange in a row and the sloped sidewall with being dehydrated pond 24 is parallel, each shaftless screw
One end of conveyer 26 is arranged at dehydration 24 bottom end of pond, and the other end is arranged at the top of continuous filter 25 so that dehydration pond
The rubbish of 24 bottoms is moved upwards with Shaftless screw conveyor 26, due to the agitation of Shaftless screw conveyor 26, in rubbish
Waste liquid can accelerate the inclined lateral side along Shaftless screw conveyor 26 and dehydration pond 24 to flow downward, and final a large amount of waste liquid is from de-
The filter opening 28 of 24 bottom of pond flows out；Rubbish is delivered to the top of continuous filter 25 by Shaftless screw conveyor 26, and fall into simultaneously
The bottom of continuous filter 25, filter opening 28 of the remaining waste liquid under gravity from 25 bottom of continuous filter flows out in rubbish.
The percolate flowed out from 16 bottom of percolating device is collected by filtrate collecting tank 15, while the discharge of centrifugal dehydrator 11
Waste liquid is also collected by filtrate collecting tank 15；The draining pump 19 of 15 bottom of filtrate collecting tank connection extracts useless in filtrate collecting tank 15
Liquid, waste liquid are transported under the action of 19 draft of draining pump in filter 18, by 15 bottom of filtrate collecting tank when waste liquid is extracted out
The filter screen 30 of setting filters；When waste liquid by filter 18 filtering after, be sent to atomizer 20 and be directed onto waste incineration
In stove 14, according to the combustion case in waste incinerator 14, adjust pressure regulator valve 23 and spray waste liquid so as to change atomizer 20
Amount enables atomizer 20 to spray the organic substance in waste liquid by 14 completely burned of waste incinerator, reduces wastewater treatment capacity
The utilization rate of rubbish is improved simultaneously.
It is percolated the house refuse completed and is grabbed in waste incinerator 14 by the grab bucket 17 of 16 top of percolating device and burnt,
The residue discharged in centrifugal dehydrator 11 simultaneously is also transported in waste incinerator 14；Auxiliary combustion equipment in waste incinerator 14
22 can help rubbish to burn, and the biogas in collecting methane tank 9 can be also delivered in waste incinerator 14, promote the complete of rubbish
Full burning.
When filter 18 filters waste liquid simultaneously, the impurity filtered out is discharged by scum pipe 21, and input diafiltration dress again
In putting 16, the utilization rate of rubbish is improved；The heat shield 29 being socketed outside atomizer 20, can effectively reduce atomizer 20 by
Heat radiation, extend the service life of atomizer 20；The exhaust fan 27 that 16 top of percolating device is set, can be by percolating device
The foul smell that rubbish generates in 16 is taken away, and there is the gases such as the methane generated after rubbish fermentation in foul smell, and 27 energy of exhaust fan will be smelly
Gas is collected, and for the conveying of air in waste incinerator 14, reduces the energy recycled while environmental pollution in rubbish
Source substance.
Claims (9)
1. kitchen castoff and consumer waste incineration coprocessing system, it is characterised in that：Including kitchen castoff collecting tank
(1), on kitchen castoff collecting tank (1) scalping (2) is connected with through pipeline；Thick slag pipe (3) and discharge nozzle are connected in scalping (2)
(4), it is connected with pulverizer (5) on discharge nozzle (4)；Desander (6) is connected with by pipeline on pulverizer (5), on desander (6)
Biogas generating device (7) is connected with by pipeline；Collecting methane tank is connected with by biogas pipe (8) on biogas generating device (7)
(9), centrifugal dehydrator (11) is connected with by residue pipe (10) on biogas generating device (7)；The bottom end of centrifugal dehydrator (11)
Conveyer belt (12) is provided with, drainpipe (13) is connected on centrifugal dehydrator (11)；One end of conveyer belt (12) is provided with rubbish
Incinerator (14), one end of drainpipe (13) are provided with filtrate collecting tank (15)；The side setting of the waste incinerator (14)
There is percolating device (16), be provided with grab bucket (17) above percolating device (16), percolating device (16) is positioned at filtrate collecting tank (15)
Top；Filter (18) is connected with by pipeline on filtrate collecting tank (15), draining pump (19) is connected on pipeline；The filtering
Atomizer (20) is connected with by pipeline on device (18), filter (18) bottom is connected with scum pipe (21).
2. according to kitchen castoff described in claim 1 and consumer waste incineration coprocessing system, it is characterised in that：The rubbish
Auxiliary combustion equipment (22) is provided in rubbish incinerator (14), auxiliary combustion equipment (22) is connect with collecting methane tank (9).
3. according to kitchen castoff described in claim 1 and consumer waste incineration coprocessing system, it is characterised in that：The mistake
Pressure regulator valve (23) is connected on pipeline between filter (18) and atomizer (20).
4. kitchen castoff according to claim 1 and consumer waste incineration coprocessing system, it is characterised in that：It is described
Including being dehydrated pond (24), the side side wall of dehydration pond (24) is inclined to set percolating device (16), is dehydrated pond (24) sloped sidewall
Side be connected with continuous filter (25)；Multiple Shaftless screw conveyors being distributed side by side are provided in dehydration pond (24)
(26), one end of each Shaftless screw conveyor (26) is arranged at dehydration pond (24) bottom end, each Shaftless screw conveyor
(26) the other end is arranged at the top of continuous filter (25)；The bottom end of dehydration pond (24) and continuous filter (25) is equipped with filter
Hole (28).
5. kitchen castoff according to claim 1 and consumer waste incineration coprocessing system, it is characterised in that：It is described
Exhaust fan (27) is provided with above percolating device (16).
6. kitchen castoff according to claim 4 and consumer waste incineration coprocessing system, it is characterised in that：It is described
The aperture of filter opening (28) is 50~80mm.
7. kitchen castoff according to claim 4 and consumer waste incineration coprocessing system, it is characterised in that：It is described
Shaftless screw conveyor (26) is parallel with the sloped sidewall for being dehydrated pond (24).
8. kitchen castoff according to claim 1 and consumer waste incineration coprocessing system, it is characterised in that：It is described
Atomizer (20) is arranged in waste incinerator (14), and heat shield (29) is socketed on the outside of atomizer (20).
9. the kitchen castoff according to any claim in claim 1 to 8 cooperates with processing system with consumer waste incineration
System, it is characterised in that：Filter screen (30) is provided in the filtrate collecting tank (15), filter screen (30) is arranged on filtrate collecting tank
(15) bottom end.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721616185.4U CN207471540U (en) | 2017-11-28 | 2017-11-28 | Kitchen castoff and consumer waste incineration coprocessing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721616185.4U CN207471540U (en) | 2017-11-28 | 2017-11-28 | Kitchen castoff and consumer waste incineration coprocessing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207471540U true CN207471540U (en) | 2018-06-08 |
Family
ID=62259911
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721616185.4U Active CN207471540U (en) | 2017-11-28 | 2017-11-28 | Kitchen castoff and consumer waste incineration coprocessing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207471540U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110319446A (en) * | 2019-06-20 | 2019-10-11 | 安徽蓝鼎环保能源科技有限公司 | A kind of landfill leachate collection drainage device |
-
2017
- 2017-11-28 CN CN201721616185.4U patent/CN207471540U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110319446A (en) * | 2019-06-20 | 2019-10-11 | 安徽蓝鼎环保能源科技有限公司 | A kind of landfill leachate collection drainage device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204523755U (en) | A kind of food waste treatment device | |
| CN204534597U (en) | A kind of changing food waste CIU | |
| CN103398383A (en) | Solid waste combustion system | |
| CN103483014B (en) | The dry treatment system of meal kitchen rubbish from cooking resource | |
| CN111036643A (en) | Method for cooperatively treating kitchen waste, household garbage and sludge of sewage plant | |
| CN105757677A (en) | Intelligent garbage treatment system with multiple gas circulation function | |
| CN102794104A (en) | Biological deodorization filter tower capable of automatically replacing and adding filter material and biological deodorization method | |
| KR100851948B1 (en) | Apparatus and method for drying organic sludge | |
| KR102090026B1 (en) | Wastewater treatment system of zero liquid discharge | |
| CN207471540U (en) | Kitchen castoff and consumer waste incineration coprocessing system | |
| CN102220232B (en) | Mechanical material discharge acidification anaerobic tank | |
| CN104438297B (en) | A kind of method and apparatus processing organic waste | |
| JP2011177637A (en) | Treatment system and treatment method for organic waste | |
| CN204644097U (en) | Sub-pressure high-efficient pyrolysis device | |
| CN211247719U (en) | Processing system for various solid wastes in circulating industrial park | |
| CN207429802U (en) | Garbage incinerating power plant is percolated liquid processing device | |
| CN206300207U (en) | A kind of processing unit of anaerobic degradation rubbish | |
| CN102417287A (en) | Sludge treatment system and method | |
| CN110564592A (en) | Field operation waste treatment integration container | |
| CN206661886U (en) | The system for handling house refuse | |
| CN204417362U (en) | A kind of apparatus for disposing of food waste | |
| CN204648266U (en) | Mud or garbage disposal incinerator system | |
| CN216203361U (en) | Domestic waste innocent treatment device | |
| CN207815343U (en) | Rubbish incinerator feeding dewatering system | |
| CN213295197U (en) | Cement production system with incineration of liquid waste |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |