CN106944463A - A kind of scattered domestic garbage resource utilizes equipment - Google Patents
A kind of scattered domestic garbage resource utilizes equipment Download PDFInfo
- Publication number
- CN106944463A CN106944463A CN201710246568.5A CN201710246568A CN106944463A CN 106944463 A CN106944463 A CN 106944463A CN 201710246568 A CN201710246568 A CN 201710246568A CN 106944463 A CN106944463 A CN 106944463A
- Authority
- CN
- China
- Prior art keywords
- rubbish
- domestic garbage
- house refuse
- hothouse
- garbage resource
- 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.)
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Links
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 77
- 238000012216 screening Methods 0.000 claims abstract description 24
- 239000005416 organic matter Substances 0.000 claims abstract description 23
- 229910052751 metal Inorganic materials 0.000 claims abstract description 13
- 239000002184 metal Substances 0.000 claims abstract description 13
- 238000005469 granulation Methods 0.000 claims abstract description 12
- 230000003179 granulation Effects 0.000 claims abstract description 12
- 230000008929 regeneration Effects 0.000 claims abstract description 12
- 238000011069 regeneration method Methods 0.000 claims abstract description 12
- 238000007885 magnetic separation Methods 0.000 claims abstract description 8
- 238000010438 heat treatment Methods 0.000 claims abstract description 3
- 238000002156 mixing Methods 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 230000005540 biological transmission Effects 0.000 claims description 7
- 238000012546 transfer Methods 0.000 claims description 7
- 230000008030 elimination Effects 0.000 claims description 6
- 238000003379 elimination reaction Methods 0.000 claims description 6
- 239000011229 interlayer Substances 0.000 claims description 4
- 238000002485 combustion reaction Methods 0.000 claims description 2
- 238000001035 drying Methods 0.000 abstract description 15
- 238000000855 fermentation Methods 0.000 abstract description 9
- 230000004151 fermentation Effects 0.000 abstract description 9
- 230000005611 electricity Effects 0.000 abstract description 5
- 239000000446 fuel Substances 0.000 abstract description 5
- 238000003756 stirring Methods 0.000 abstract description 5
- 238000009264 composting Methods 0.000 abstract description 3
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 3
- 230000009471 action Effects 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract description 2
- 239000007787 solid Substances 0.000 abstract description 2
- 238000003860 storage Methods 0.000 abstract description 2
- -1 this is flammable Substances 0.000 abstract 1
- 238000010564 aerobic fermentation Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- 238000010792 warming Methods 0.000 description 3
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 239000010791 domestic waste Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000003643 water by type 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
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/46—Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Equipment is utilized the invention discloses a kind of scattered domestic garbage resource, house refuse and strain enter from rubbish cast hopper, enter house refuse through rubbish conveyer belt and dry deodoriser, house refuse is rolled forward under heating, stirring action, dried under the conditions of suitable high-temperature aerobic, fermentation process, so as to effectively realize the drying of solid mixt;Dried object enters metal Magnet Separater through hopper, rubbish conveyer belt and carries out magnetic separation, will enter screening plant through rubbish conveyer belt after the heavy metal separation in composting;Oversize and screenings are separated into after refinement screening, oversize enters Granulation Equipments through rubbish conveyer belt, as flammable organic matter fuel, this is flammable, and organic matter fuel part is converted into high heat energy steam for house refuse drying deodoriser hot fermentation drying for special regeneration organic matter burning boiler;Remainder regenerates organic matter to be disposed into burning electricity generation, or temporarily landfill storage.
Description
Technical field
Equipment is utilized the present invention relates to environmental technology field, more particularly to a kind of scattered domestic garbage resource.
Background technology
With the increasing of Development of China's Urbanization, the intractable environmental problem that application of city life garbage is faced as Development of China's Urbanization it
One.Especially recently as the proposition in " blue mountains and green waters " effect epoch, the life under urban and rural environment comprehensive regulation strategic framework
Refuse collection, transport, focus on the mainstream market as domestic rubbish disposal, so further increasing county, city-level life
The pressure of rubbish final process disposal site.
Current China mainly has for the terminal processes disposing technique of house refuse:Consumer waste filling and embedding, house refuse are burnt
Burn.As town and country rubbish receives the increasing of transhipment dynamics, the processing side that village is collected, town is transported, counties and cities fill or burned can be achieved
Formula.Township, the collection of town rubbish are imported, and cause county domain refuse landfill day amount of landfill increase, landfill yard excess is filled out, final to be not up to
The closing amount of landfill that design period has just reached, and clearly carry and prohibiting from after 2016 in national relevant law and place regulation
Only newly-built household refuse landfill sites;For the counties and cities using domestic garbage burning electricity generation, township, the collection of town rubbish are imported, and are expanded
The construction scale of burning electricity generation, but small towns rubbish, compared to domestic waste, its calorific value bottom, inorganic component content are high,
The furnace temperature of incinerator has been dragged down during burning, so that burning electricity generation amount is reduced, the overall investment return of influence project.
Small towns rubbish frequently encounters the remote villages and small towns garbage transporting in portion apart from excessive collecting transport process, and road traffic is not
Just, and garbage sludge constituent content is too high, so as to significantly increase cost of wheeling, even economically consider, part
Area does not possess the condition for collecting transhipment.
The content of the invention
The problem of run into during policy execution is focused on for current town and country refuse collection, the present invention proposes one kind
The scattered domestic garbage resources of Domestic Waste Collection transhipment and terminal handling problems are solved from domestic garbage resource, minimizing angle
Change utilizes equipment.
Therefore, the present invention provides a kind of scattered domestic garbage resource includes rubbish cast hopper, house refuse using equipment
Dry deodoriser, hopper, metal Magnet Separater, screening plant, Granulation Equipments and regeneration organic matter burning boiler;The rubbish
Rubbish cast hopper is dried deodoriser, the metal Magnet Separater with the house refuse and set with the screening plant, the screening
It is standby to be connected with the Granulation Equipments by rubbish conveyer belt;The hopper is dried under deodoriser located at the house refuse
Side.
Further, the metal Magnet Separater includes magnetic separation transfer roller and the scraper located at the magnetic separation transfer roller side.
Further, the house refuse is dried deodoriser and included between double-deck hothouse, hothouse described in two provided with steaming
Vapour heats interlayer.
Further, it is equipped with condensed water elimination pipeline below each hothouse.
Preferably, two power transmission shaft agitating devices, each power transmission shaft stirring dress are equipped with each hothouse
Put and be equipped with double-deck arc mixing blade.
Preferably, the upper strata blade of double-deck arc mixing blade is installed with blade in reverse;And each arc stirring
The radian of blade is 10~25 °.
Further, negative pressure exhausting system is provided with the hothouse.
Further, pumped vacuum systems is provided with the hothouse.
Further, the hothouse is connected with the regeneration organic matter burning boiler by steam conveying pipe, through changing
After heat, steam is converted into condensed water and discharged by condensed water elimination pipeline in hothouse.
Compared with prior art, the invention has the advantages that:
1st, after house refuse is handled by the scattered domestic garbage resource of one's duty using equipment, inert substance is ultimately formed
With regeneration organic matter fuel, so as to effectively realize, house refuse is in situ to administer decrement;
2nd, part organic matter granulation combustible decrement, volume reduction outward transport, so that outward transport quantity of refuse is effectively reduced, reduction fortune
Defeated frequency, saves and receives fortune cost, while organic matter combustible is higher compared to composting calorific value, generating efficiency is higher;
3rd, steam is set to heat interlayer between double-deck hothouse, house refuse is rotating in same direction axle in whole drying process
Impetus under seethe forward, so as to realize that the continuous mixing of rubbish is seethed, warming interface is constantly updated, and is favorably improved dry
Dry efficiency;
The 4th, negative pressure exhausting system is set in hothouse, so as to realize that moisture vaporization temperature is reduced under condition of negative pressure, simultaneously
Ensure that house refuse dries hot fermentation condition of the deodoriser drying temperature at 55~65 DEG C;
5th, upper strata blade and blade, so as to realize that the overall plug-flow of rubbish is reciprocal, are effectively increased rubbish in reverse installation
Rubbish dries deodoriser effective residence time in house refuse;
The 6th, pumped vacuum systems is set in hothouse, reactor temperature is effectively controlled, under certain vacuum degree condition, is increased
Plus refuse moisture dries evaporation rate, reactor temperature is reduced, the condition of high-temperature aerobic fermentation is met;
7th, hot fermentation microorganism is contained in inanimate matter under the sieve after screened equipment screening, thus in house refuse through rubbish
Rubbish cast hopper is together added before entering system with part screenings, so as to ensure bacterium of the rubbish during high-temperature aerobic fermentation
Plant amount.
Brief description of the drawings
Technical scheme in order to illustrate more clearly the embodiments of the present invention, below will be to that will make needed for embodiment description
Accompanying drawing is briefly described, it should be apparent that, drawings in the following description are only some embodiments of the present invention, for
For those of ordinary skill in the art, on the premise of not paying creative work, other can also be obtained according to these accompanying drawings
Accompanying drawing.
Fig. 1 is the structural representation of the present invention, wherein:
Rubbish cast hopper 1, rubbish conveyer belt 2, house refuse dry deodoriser 3, metal Magnet Separater 4, hopper 5,
Screening plant 6, Granulation Equipments 7, regeneration organic matter burning boiler 8, power transmission shaft agitating device 9, arc mixing blade 10, condensed water
Discharge tube 11, hothouse 12.
Embodiment
To make the object, technical solutions and advantages of the present invention clearer, below in conjunction with accompanying drawing to embodiment party of the present invention
Formula is described in further detail.
Referring to Fig. 1, the present embodiment provides a kind of scattered domestic garbage resource includes rubbish cast hopper 1, life using equipment
Drying garbage deodoriser 3 living, hopper 5, metal Magnet Separater 4, screening plant 6, Granulation Equipments 7 and regeneration organic matter burning
Boiler 8;The rubbish cast hopper 1 dries deodoriser 3, the metal Magnet Separater 4 and the screening with the house refuse
Equipment 6, the screening plant 6 are connected with the Granulation Equipments 7 by rubbish conveyer belt 2;The hopper 5 is located at the life
The lower section of drying garbage deodoriser 3 living.
House refuse and strain enter from rubbish cast hopper 1, and through rubbish conveyer belt 2, deodoriser is dried into house refuse
3, house refuse is rolled forward in house refuse dries deodoriser 3 under heating, stirring action, in suitable high-temperature aerobic bar
Dried under part, fermentation process, so as to effectively realize the drying of solid mixt;Dried object dries deodoriser through house refuse
The hopper 5 of 3 lower sections, rubbish conveyer belt 2 enter metal Magnet Separater 4 and carry out magnetic separation;Metal Magnet Separater 4 will mix rubbish
Enter screening plant 6 through rubbish conveyer belt 2 after heavy metal separation in rubbish;It is separated into after refinement screening under oversize and sieve
Thing, oversize includes bulky grain organic matter and combustible, and screenings is the inert substances such as inorganic dregs;Oversize is conveyed through rubbish
Band 2 enters Granulation Equipments 7, and volume reduction, decrement are realized through overcompaction, granulation, as flammable organic matter fuel, organic matter combustion that this is flammable
Expect that part is used for special regeneration organic matter burning boiler 8 and is converted into high heat energy steam for the house refuse drying high temperature of deodoriser 3
Fermentation drying;Remainder regeneration organic matter carries out outward transport and enters burning electricity generation final disposal, or in household refuse landfill sites rule
Draw organic matter landfill region and carry out temporarily landfill storage.
The house refuse, which dries deodoriser 3, to be included provided with steam adding between double-deck hothouse 12, hothouse 12 described in two
Thermofin, house refuse is seethed forward during whole middle temperature is dried under the impetus for rotating in same direction axle, layer and realize
The continuous mixing of rubbish is seethed, and warming interface is constantly updated;Negative pressure exhausting system (not shown) is provided with hothouse 12, so that real
Moisture vaporization temperature is reduced under present condition of negative pressure, while ensureing that house refuse dries the drying temperature of deodoriser 3 at 55~65 DEG C
Hot fermentation condition;Two power transmission shaft agitating devices 9, each power transmission shaft stirring are equipped with each hothouse 12
Double-deck arc mixing blade 10 is equipped with device 9;The upper strata blade of double-deck arc mixing blade 10 is with blade in reverse
Install;And the radian of each arc mixing blade 10 is 10~25 °, so as to realize that the overall plug-flow of rubbish is reciprocal, it is effectively increased
Rubbish dries the effective residence time of deodoriser 3 in house refuse;Pumped vacuum systems (not shown), effectively control are set in hothouse 12
Reactor temperature processed, under certain vacuum degree condition, increase refuse moisture dries temperature in evaporation rate, reduction reactor
Degree, meets the condition of high-temperature aerobic fermentation;Each lower section of the hothouse 12 is equipped with condensed water elimination pipeline 11, the drying
Room 12 is connected with the regeneration organic matter burning boiler 8 by steam conveying pipe, after heat exchange steam be converted into condensed water by
Condensed water elimination pipeline 11 is discharged.
The metal Magnet Separater 4 includes magnetic separation transfer roller 41 and the scraper 42 located at the side of magnetic separation transfer roller 41, magnetic
Select transfer roller 41 to adsorb metal garbage, heavy metal substance is scraped through scraper 9 and segregates into rubbish conveyer belt 2, screening is transported to outside and is set
Standby 6.
Contain hot fermentation microorganism in the screenings of screening plant 6, system can be entered through rubbish cast hopper 1 in house refuse
Together added with part screenings before system.
To sum up, after house refuse is handled by the scattered domestic garbage resource of one's duty using equipment, inertia is ultimately formed
Material and regeneration organic matter fuel, so that effectively realizing house refuse original position administers decrement;Part organic matter granulation is flammable
Thing decrement, volume reduction outward transport, so as to be effectively reduced outward transport quantity of refuse, reduction transport frequency is saved and receives fortune cost, while organic
Matter combustible is higher compared to composting calorific value, and generating efficiency is higher;Steam is set to heat interlayer, life between double-deck hothouse
Rubbish is seethed forward in whole drying process under the impetus for rotating in same direction axle, so as to realize that the continuous mixing of rubbish is turned over
Rise, warming interface is constantly updated, and is favorably improved drying efficiency;Negative pressure exhausting system is set in hothouse, so as to realize negative
Moisture vaporization temperature is reduced under the conditions of pressure, while ensureing that house refuse is dried deodoriser drying temperature and sent out in 55~65 DEG C of high temperature
Ferment condition;Upper strata blade and blade, so as to realize that the overall plug-flow of rubbish is reciprocal, are effectively increased rubbish and existed in reverse installation
House refuse dries deodoriser effective residence time;Pumped vacuum systems is set in hothouse, reactor temperature is effectively controlled,
Under certain vacuum degree condition, increase refuse moisture dries evaporation rate, reduces reactor temperature, meets high-temperature aerobic fermentation
Condition;Contain hot fermentation microorganism in inanimate matter under sieve after screened equipment screening, thus in house refuse through rubbish
Cast hopper is together added before entering system with part screenings, so as to ensure strain of the rubbish during high-temperature aerobic fermentation
Amount.
The foregoing is only presently preferred embodiments of the present invention, be not intended to limit the invention, it is all the present invention spirit and
Within principle, any modifications, equivalent substitutions and improvements made etc. should be included within the scope of the present invention.
Claims (9)
1. a kind of scattered domestic garbage resource utilizes equipment, it is characterised in that done including rubbish cast hopper (1), house refuse
Dry deodoriser (3), hopper (5), metal Magnet Separater (4), screening plant (6), Granulation Equipments (7) and regeneration organic matter combustion
Burning boiler (8);The rubbish cast hopper (1) dries deodoriser (3), the metal Magnet Separater (4) with the house refuse
It is connected with the screening plant (6), the screening plant (6) with the Granulation Equipments (7) by rubbish conveyer belt (2);Institute
State the lower section that hopper (5) dries deodoriser (3) located at the house refuse.
2. a kind of scattered domestic garbage resource according to claim 1 utilizes equipment, it is characterised in that the metallic magnetic
Selecting separator (4) includes magnetic separation transfer roller (41) and the scraper (42) located at magnetic separation transfer roller (41) side.
3. a kind of scattered domestic garbage resource according to claim 1 utilizes equipment, it is characterised in that the life rubbish
Rubbish, which dries deodoriser (3), to be included heating interlayer provided with steam between double-deck hothouse (12), hothouse described in two (12).
4. a kind of scattered domestic garbage resource according to claim 3 utilizes equipment, it is characterised in that each described dry
Condensed water elimination pipeline (11) is equipped with below dry room (12).
5. a kind of scattered domestic garbage resource according to claim 3 utilizes equipment, it is characterised in that each described dry
It is equipped with dry room (12) on two power transmission shaft agitating devices (9), each power transmission shaft agitating device (9) and is equipped with double-deck arc
Shape mixing blade (10).
6. a kind of scattered domestic garbage resource according to claim 5 utilizes equipment, it is characterised in that double-deck arc is stirred
The upper strata blade and blade for mixing blade (10) are installed in reverse;And the radian of each arc mixing blade (10) be 10~
25°。
7. a kind of scattered domestic garbage resource according to claim 3 utilizes equipment, it is characterised in that the hothouse
(12) negative pressure exhausting system is provided with.
8. a kind of scattered domestic garbage resource according to claim 3 utilizes equipment, it is characterised in that the hothouse
(12) pumped vacuum systems is provided with.
9. a kind of scattered domestic garbage resource according to claim 3 utilizes equipment, it is characterised in that the hothouse
(12) it is connected with the regeneration organic matter burning boiler (8) by steam conveying pipe, after heat exchange, hothouse (12) interior steam
Condensed water is converted into be discharged by condensed water elimination pipeline (11).
Priority Applications (1)
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CN201710246568.5A CN106944463A (en) | 2017-04-15 | 2017-04-15 | A kind of scattered domestic garbage resource utilizes equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201710246568.5A CN106944463A (en) | 2017-04-15 | 2017-04-15 | A kind of scattered domestic garbage resource utilizes equipment |
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Publication Number | Publication Date |
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CN106944463A true CN106944463A (en) | 2017-07-14 |
Family
ID=59476220
Family Applications (1)
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CN201710246568.5A Pending CN106944463A (en) | 2017-04-15 | 2017-04-15 | A kind of scattered domestic garbage resource utilizes equipment |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107537659A (en) * | 2017-09-26 | 2018-01-05 | 徐美琴 | A kind of equipment for handling rubbish |
CN109013038A (en) * | 2018-08-29 | 2018-12-18 | 深圳市旭发智能科技有限公司 | A kind of waste disposal method |
CN109107743A (en) * | 2018-08-29 | 2019-01-01 | 深圳市旭发智能科技有限公司 | A kind of refuse disposal system |
CN111051478A (en) * | 2017-08-31 | 2020-04-21 | 株式会社下濑微生物研究所 | Fuel processing device and fuel processing method based on fermentation drying of processing object |
CN111094522A (en) * | 2017-09-19 | 2020-05-01 | 株式会社下濑微生物研究所 | Fuel manufacturing device and method for biomass burner |
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CN106269235A (en) * | 2016-08-29 | 2017-01-04 | 中冶北方(大连)工程技术有限公司 | A kind of concentration magnetic separation dehydration equipment |
CN106440663A (en) * | 2016-12-23 | 2017-02-22 | 郑州搜趣信息技术有限公司 | Double spiral type chemical powder stock microwave drying device |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
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CN111051478A (en) * | 2017-08-31 | 2020-04-21 | 株式会社下濑微生物研究所 | Fuel processing device and fuel processing method based on fermentation drying of processing object |
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CN111094522A (en) * | 2017-09-19 | 2020-05-01 | 株式会社下濑微生物研究所 | Fuel manufacturing device and method for biomass burner |
CN111094522B (en) * | 2017-09-19 | 2021-09-10 | 株式会社下濑微生物研究所 | Fuel manufacturing device and method for biomass burner |
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CN109013038A (en) * | 2018-08-29 | 2018-12-18 | 深圳市旭发智能科技有限公司 | A kind of waste disposal method |
CN109107743A (en) * | 2018-08-29 | 2019-01-01 | 深圳市旭发智能科技有限公司 | A kind of refuse disposal system |
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Application publication date: 20170714 |