CN106077052A - Life refuse processing method - Google Patents
Life refuse processing method Download PDFInfo
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- CN106077052A CN106077052A CN201610696345.4A CN201610696345A CN106077052A CN 106077052 A CN106077052 A CN 106077052A CN 201610696345 A CN201610696345 A CN 201610696345A CN 106077052 A CN106077052 A CN 106077052A
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- house refuse
- waste disposal
- raw material
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- disposal method
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- 238000003672 processing method Methods 0.000 title abstract description 9
- 238000000034 method Methods 0.000 claims abstract description 38
- 230000008569 process Effects 0.000 claims abstract description 25
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 24
- 239000003610 charcoal Substances 0.000 claims abstract description 21
- 238000005336 cracking Methods 0.000 claims abstract description 16
- 238000000855 fermentation Methods 0.000 claims abstract description 16
- 230000004151 fermentation Effects 0.000 claims abstract description 16
- 239000002994 raw material Substances 0.000 claims abstract description 16
- 239000002699 waste material Substances 0.000 claims abstract description 16
- 239000004033 plastic Substances 0.000 claims abstract description 11
- 229920003023 plastic Polymers 0.000 claims abstract description 11
- 229910052751 metal Inorganic materials 0.000 claims abstract description 10
- 239000002184 metal Substances 0.000 claims abstract description 10
- 239000000843 powder Substances 0.000 claims abstract description 8
- 238000010298 pulverizing process Methods 0.000 claims abstract description 6
- 239000007921 spray Substances 0.000 claims abstract description 6
- 238000006243 chemical reaction Methods 0.000 claims description 7
- 238000000197 pyrolysis Methods 0.000 claims description 7
- 241000894006 Bacteria Species 0.000 claims description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 5
- 239000001301 oxygen Substances 0.000 claims description 5
- 229910052760 oxygen Inorganic materials 0.000 claims description 5
- 210000004243 sweat Anatomy 0.000 claims description 5
- 230000035800 maturation Effects 0.000 claims description 3
- 230000007613 environmental effect Effects 0.000 claims description 2
- 238000004064 recycling Methods 0.000 abstract description 3
- 229910052799 carbon Inorganic materials 0.000 description 7
- 239000007789 gas Substances 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 239000002893 slag Substances 0.000 description 5
- 239000004575 stone Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 230000002159 abnormal effect Effects 0.000 description 4
- 238000004332 deodorization Methods 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 230000006798 recombination Effects 0.000 description 4
- 238000005215 recombination Methods 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 3
- 239000002737 fuel gas Substances 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 241000186361 Actinobacteria <class> Species 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 241000233866 Fungi Species 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000004035 construction material Substances 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- -1 husky Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000003895 organic fertilizer Substances 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 230000035943 smell Effects 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- GCNLQHANGFOQKY-UHFFFAOYSA-N [C+4].[O-2].[O-2].[Ti+4] Chemical compound [C+4].[O-2].[O-2].[Ti+4] GCNLQHANGFOQKY-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000001066 destructive effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000686 essence Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 229960003883 furosemide Drugs 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 230000005070 ripening Effects 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F9/00—Fertilisers from household or town refuse
- C05F9/04—Biological compost
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Molecular Biology (AREA)
- Materials Engineering (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses one way of life waste disposal method, comprise the steps: coarse pulverization: house refuse crushed;Fermentation: spray strain in the house refuse after broken and carry out fermentation process;Dehydrate: add the house refuse after hot fermentation, makes the moisture in house refuse evaporate;Fine powder is broken: again crush dried rubbish;Sorting: fine powder rubbish after broken is divided into this three class of plastics, charcoal raw material and metal;The charcoal raw material sub-elected carries out anaerobic cracking process.The life refuse processing method using the present invention processes house refuse, house refuse is divided into callable plastics, metal and charcoal raw material after treatment, charcoal raw material uses anaerobic cracking to process, after process, house refuse realizes 100% recycling, non-secondary pollution, practicality is the highest.
Description
Technical field
The invention belongs to technical field of waste treatment, relate to one way of life waste disposal method.
Background technology
Along with the high speed development of China's economic construction, urbanization process speed is constantly accelerated, and living standards of the people constantly carry
Height, the substantial increase of solid waste particularly domestic waste can not get dealing carefully with, and pollution on the environment is the most serious.
At present, some cities of China begin with burning disposal rubbish or utilization is burnt away the refuse heat energy power-generating or confession
Heat, the ratio of garbage disposal more thoroughly, but its shortcoming is the most prominent, i.e. construction investment scale is big, and the investment payback time is long, with
Time combustion process in produce second time and pollute, " two English " toxicity that particularly in rubbish, the burning of a large amount of plastics produces very greatly,
There is carcinogenic danger.To this end, necessary design one way of life waste disposal method, use this life refuse processing method to life
Rubbish processes, to overcome the problem of insurmountable secondary pollution in conventional treatment.
Summary of the invention
It is an object of the invention to provide a kind of practicality height, the life refuse processing method of non-secondary pollution.
In order to solve above-mentioned technical problem, the technical solution used in the present invention is: one way of life waste disposal method, including
Following steps:
A. coarse pulverization: house refuse is crushed;
B. fermentation: spray strain in the house refuse after broken and carry out fermentation process;
C. dehydrate: add the house refuse after hot fermentation, makes the moisture in house refuse evaporate;
D. fine powder is broken: again crush dried rubbish;
E. sorting: fine powder rubbish after broken is divided into this three class of plastics, charcoal raw material and metal.
Further, sprayed in the house refuse of strain is placed on reaction chamber and fermented, by the intensification of house refuse
Process, sweat is divided into three phases: initial period, hot stage and maturation stage.
Further, described strain is main line bacterium.
Further, anaerobic cracking process is carried out in described charcoal raw material being sent into anaerobic pyrolysis furnace.
Further, it is heated up to 100 DEG C before in described charcoal raw material sends into anaerobic pyrolysis furnace.
Further, close, temperature conditions be 400 DEG C to 600 DEG C without the environmental condition of flame and oxygen under carry out institute
State anaerobic cracking.
Further, described coarse pulverization step is carried out after described house refuse being carried out deodorization process again.
The method have the benefit that the life refuse processing method using the present invention processes house refuse, house refuse is through place
Being divided into callable plastics, metal and charcoal raw material after reason, charcoal raw material uses anaerobic cracking to process, due to nothing
Oxygen cracking will not destroy the molecule of hydrocarbons and other refuse, can promote the decomposition of molecular recombination, the Organic substance warp in rubbish
Crossing anaerobic cracking formation forming gas to use for the external world, remaining solid biologic carbon is made standard charcoal finished product or is used as
The dispensing of organic fertilizer, husky, stone inorganic matter is used for making construction material, it is achieved 100% recycling, and non-secondary pollution is practical
Property high.
Accompanying drawing explanation
Fig. 1 is the flow chart of the life refuse processing method of the embodiment of the present invention.
Detailed description of the invention
Below in conjunction with the accompanying drawing of the present invention, the technical scheme in the embodiment of the present invention is clearly and completely described,
Obviously, described embodiment is only a part of embodiment of the present invention rather than whole embodiments.Based in the present invention
Embodiment, the every other embodiment that those of ordinary skill in the art are obtained under not making creative work premise, all
Belong to the scope of protection of the invention.
As it is shown in figure 1, the flow chart of the one way of life waste disposal method of the present embodiment.This life refuse processing method bag
Include following steps:
Step 1: deodorization processes
House refuse carries out taste removal process after entering factory during unloading, and makes waste odours not exhale, in factory's week
Do not have abnormal flavour to produce outside exclosure district 500 rice diameter scope, unique produce abnormal smells from the patient source simply rubbish enter factory before in transit, because of
This coverage is minimum.
Step 2: coarse pulverization
Coarse crushing equipment is used to crush carrying out the house refuse that deodorization processed.
Step 3: fermentation
House refuse after broken is sent in reaction chamber, sprays strain to house refuse during sending into, strain with
Water, by the proportioning (change determine because season is different with weather) of 1000:2000, about sprays proportioning strain in each reaction chamber
2000-3000 kilogram, the house refuse having sprayed strain carries out fermentation process, decision design, the strain of sprinkling in reaction chamber
For main line bacterium.
By the temperature-rise period of house refuse, sweat is divided into three phases: initial period, hot stage and ripening rank
Section.Initial period: the temperature in reaction chamber is about Jun Heng with outdoor temperature, mesophilic bacteria, actinomycetes, yeast and fungus are decomposed
Glucose degradable in Organic substance, fat and carbohydrate, heat produced by heat resolve promotes strip-like-shaped heap material
Temperature rises, and when temperature is raised to 40-50 DEG C, then enters the second stage i.e. hot stage of rubbish fermentation process.Now, rubbish rises
The microbes natural death in stage beginning, the substitute is a series of Thermophilic Bacteria, and produced by its growth, heat enters again one
Step rises to 70 DEG C again reaction the temperature inside the box, in the rubbish that temperature is 60-70 DEG C, in addition to some spores, and all of cause of disease
Microorganism all can be dead at short notice.When Organic substance has been degraded substantially, Thermophilic Bacteria will stop raw owing to lacking nutriment
Long, heat stops the most therewith, and rubbish temperature will be gradually reduced due to heat radiation.Now, rubbish fermentation process is just entered the phase III:
Maturation stage.In rubbish after the cooling period, a series of new microorganisms (mainly fungus phase actinomycetes), have by means of remaining
Machine thing (including the antibacterial residuum died) and grow, be finally completed sweat.It is therefore contemplated that sweat is antibacterial life
Long, dead process, is also the process of rubbish temperature raising and lowering, and house refuse, after strain fermentation, need to be entered with fermenting case
Row second time rolling is to have met the oxygen fermentation needs to air.Now the volume of rubbish is about condensed to original volume 50%, then warp
After rolling several times, along with the decline of temperature, its temperature is reduced to about 25 35 DEG C by original about 60 70 DEG C, is then used
The rubbish handled well is put into next station by conveyer belt.
Step 4: dehydrate
House refuse after using dehydrator to add hot fermentation, makes the moisture in house refuse evaporate.
Step 5: fine powder is broken
Dried rubbish, through scalping, middle sieve, a series of screening of dusting cover Three Estate, uses large-scale spiral disintegrating machine to enter
Row crushes again.
Step 6: sorting
Fine powder refuse classification after broken is gone out plastics, charcoal raw material and magneticly elects this three class of metal.The plastics separated
Carry out plastic reclaimed, produce plastic product;The metal separated recycles;The charcoal raw material separated is warmed to
100 DEG C, carrying out anaerobic cracking process in being then fed into anaerobic pyrolysis furnace, anaerobic cracking generates charcoal, fuel gas after processing
And residue.
Anaerobic cracking processes: use " pyrolysis low in calories " Particular craft of relative low temperature to make refuse at special enclosed environment
Under the conditions of, do not have hydrocarbonization in the environment of flame and oxygen under the conditions of utilizing temperature 400 DEG C to 600 DEG C during pyrolysis
Compound and other waste materials anaerobics crack, promote molecular recombination decomposition and be converted into gas and basic element.All gas
Body is converted into carbon monoxide, hydrogen, methane and a small amount of carbon dioxide and produces efficient, safe and reliable flammable forming gas,
Toxic gas will not be produced, flammable forming gas through Roots's machine extraction pipe carry storage tank, remaining solid residue be biological carbon,
The side-products such as slag sand, stone and metal, completely after cracking, slag tap through tube seat helical axis.
The process of fuel gas, biological carbon, slag sand, stone, metal etc.: carbon monoxide, hydrogen, methane and a small amount of titanium dioxide
Carbon, flammable forming gas, passed through filtration and desulphurization and denitration spray system, catalysis system, is carried out by closed conduct conveying storage tank
Storing and use for the external world, as being supplied to the turbine in power plant to generate electricity, electricity provides electrical network to use;Biological carbon and slag
Being transported to pulverizer and wind sorting cyclone collector cloth bag recovery use at storage tank through enclosing coil device, charcoal makes standard
Charcoal finished product, or can use the biological carbon making fertilizer to be transported to make the use of fertile workshop;Residue slag sand, stone etc. are transported to make brick workshop and use.
And carry out combustion waste by incineration, under aerobic existence condition flame can cause heavy damage Hydrocarbon and its
The molecule of his refuse destroys, and molecular recombination creates a large amount of harmful substance while being converted into the fuel gas of very poor efficiency,
Such as two English, furosemide feeding etc..
To sum up, the life refuse processing method of the present invention, deodorization process can be carried out before process, during process, do not have abnormal flavour to produce
Raw, process ordorless abnormal smells from the patient around plant area, air quality is good;Treated house refuse produce callable plastics, metal with
And charcoal raw material, charcoal raw material uses anaerobic cracking to process, and owing to anaerobic cracking has unusual effect, it did not both have
There is the molecule of destructive hydrocarbons and other refuse, the decomposition of molecular recombination can be promoted, if the Organic substance of rubbish is through anaerobic
Cracking out forming gas, remaining solid biologic carbon is made standard charcoal finished product or is used as the dispensing of organic fertilizer, husky,
Stone inorganic matter is used for making construction material, completely can be with 100% recycling after such domestic rubbish disposal, non-secondary pollution,
High financial profit.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all essences in the present invention
Within god and principle, any modification, equivalent substitution and improvement etc. made, should be included within the scope of the present invention.
Claims (7)
1. one way of life waste disposal method, it is characterised in that comprise the steps:
A. coarse pulverization: house refuse is crushed;
B. fermentation: spray strain in the house refuse after broken and carry out fermentation process;
C. dehydrate: add the house refuse after hot fermentation, makes the moisture in house refuse evaporate;
D. fine powder is broken: again crush dried rubbish;
E. sorting: fine powder rubbish after broken is divided into this three class of plastics, charcoal raw material and metal.
One way of life waste disposal method the most according to claim 1, it is characterised in that sprayed the house refuse of strain
Fermenting in being placed on reaction chamber, by the temperature-rise period of house refuse, sweat is divided into three phases: initial period, height
Thermophase and maturation stage.
One way of life waste disposal method the most according to claim 1 and 2, it is characterised in that described strain is main line bacterium.
One way of life waste disposal method the most according to claim 1, it is characterised in that described charcoal raw material is sent
Anaerobic cracking process is carried out in entering anaerobic pyrolysis furnace.
One way of life waste disposal method the most according to claim 4, it is characterised in that described charcoal raw material is sent into
It is heated up to 100 DEG C before in anaerobic pyrolysis furnace.
One way of life waste disposal method the most according to claim 4, it is characterised in that close, temperature conditions be 400
DEG C to 600 DEG C without carrying out described anaerobic cracking under the environmental condition of flame and oxygen.
One way of life waste disposal method the most according to claim 1, it is characterised in that described house refuse is removed
Described coarse pulverization step is carried out again after smelly process.
Priority Applications (1)
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CN201610696345.4A CN106077052A (en) | 2016-08-19 | 2016-08-19 | Life refuse processing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610696345.4A CN106077052A (en) | 2016-08-19 | 2016-08-19 | Life refuse processing method |
Publications (1)
Publication Number | Publication Date |
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CN106077052A true CN106077052A (en) | 2016-11-09 |
Family
ID=58070841
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CN201610696345.4A Pending CN106077052A (en) | 2016-08-19 | 2016-08-19 | Life refuse processing method |
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Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106513416A (en) * | 2016-10-31 | 2017-03-22 | 南开大学 | A technical method for mixed refuse sorting and deodorizing |
CN106623339A (en) * | 2015-10-28 | 2017-05-10 | 上海金惠环保科技有限公司 | A fuel conversion treatment method for urban domestic waste and an additive applied for urban domestic waste treatment |
CN107716523A (en) * | 2017-11-13 | 2018-02-23 | 衢州市膜力环保科技有限公司 | The method and apparatus that a kind of domestic garbage resource utilizes |
CN108006653A (en) * | 2017-12-01 | 2018-05-08 | 贺玉婷 | The processing unit of household kitchen garbage bio-waste |
CN108787692A (en) * | 2017-04-30 | 2018-11-13 | 长沙恒凯电子科技有限公司 | A kind of waste disposal method |
CN109226171A (en) * | 2017-07-10 | 2019-01-18 | 湖南万容科技股份有限公司 | A kind of domestic garbage comprehensive recycling processing method |
CN109226213A (en) * | 2017-07-10 | 2019-01-18 | 湖南万容科技股份有限公司 | A kind of domestic garbage comprehensive recycling processing method |
CN109877131A (en) * | 2017-12-06 | 2019-06-14 | 江苏洪诚健康科技有限公司 | A kind of decompression fermentation drying device |
CN111036650A (en) * | 2019-12-20 | 2020-04-21 | 安徽家齐物业管理有限公司 | Novel environment-friendly household garbage treatment method |
CN111718876A (en) * | 2020-06-29 | 2020-09-29 | 北京中外建建筑设计有限公司 | Compound microbial agent and preparation method and application thereof |
CN114798703A (en) * | 2022-03-22 | 2022-07-29 | 中印恒盛(北京)贸易有限公司 | Municipal waste fuel production device with fermentation treatment device |
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