CN107142283A - A kind of processing method of municipal refuse - Google Patents

A kind of processing method of municipal refuse Download PDF

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Publication number
CN107142283A
CN107142283A CN201710295388.6A CN201710295388A CN107142283A CN 107142283 A CN107142283 A CN 107142283A CN 201710295388 A CN201710295388 A CN 201710295388A CN 107142283 A CN107142283 A CN 107142283A
Authority
CN
China
Prior art keywords
municipal refuse
ferment
processing method
organic matter
biogas
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.)
Pending
Application number
CN201710295388.6A
Other languages
Chinese (zh)
Inventor
魏向廷
王刚
张仁友
张仁明
聂在和
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sichuan And Ancient Cooking Vessel Environment-Friendly Engineering Co Ltd
Original Assignee
Sichuan And Ancient Cooking Vessel Environment-Friendly Engineering Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sichuan And Ancient Cooking Vessel Environment-Friendly Engineering Co Ltd filed Critical Sichuan And Ancient Cooking Vessel Environment-Friendly Engineering Co Ltd
Priority to CN201710295388.6A priority Critical patent/CN107142283A/en
Publication of CN107142283A publication Critical patent/CN107142283A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P5/00Preparation of hydrocarbons or halogenated hydrocarbons
    • C12P5/02Preparation of hydrocarbons or halogenated hydrocarbons acyclic
    • C12P5/023Methane
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P2201/00Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P2203/00Fermentation products obtained from optionally pretreated or hydrolyzed cellulosic or lignocellulosic material as the carbon source
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

The invention belongs to technical field of waste treatment, and in particular to a kind of processing method of municipal refuse;Comprise the following steps:1) sort:Municipal refuse raw material is fed through in separator, can ferment organic matter and the inanimate matter that can not ferment is sub-elected;2) crush:By the organic matter crusher in crushing of fermenting sub-elected;3) ferment:The organic matter that ferments after will be broken is added in fermentation tank, and adds zymotic fluid, lipase and cellulase, and it is 50 65 DEG C to control fermentation temperature, and pH is 68, and ferment 40 50h;4) product is handled:The biogas that fermentation is produced is transported to biogas center, and biogas slurry and biogas residue are discharged after being post-processed;The present invention proposes a kind of processing method of municipal refuse, and the organic matter that be able to will can ferment carries out degradation treatment, and factor of created gase is higher, and resource utilization is high.

Description

A kind of processing method of municipal refuse
Technical field
The invention belongs to technical field of waste treatment, and in particular to a kind of processing method of municipal refuse.
Background technology
The mankind constantly expand to natural resources exploitation and Li Yong in scale and intensity, consume the speed of resource also big It is big to accelerate, civilization on the one hand is brought to society, people's quality of life is improved, on the other hand also implies that and accelerates rubbish Increase, and rubbish is one of major reason of environmental pollution, if let drift, negligence of management and processing, it will result in Public hazards, destroy ecological environment, injure the health of people, substantially there is the following aspects:
Dumping not only occupies cultivated land, and goes back contaminated soil and crops, because chemical products content is more come in rubbish The even upper a century of many decades adds toxic component and heavy metal with which, these arable lands all without degraded after height, landfill Use value is just lost, rubbish oozes drip polluted underground water through rainwater or enters surface water, causes water pollution, 80% stream Row disease is all therefore propagated, and causes rivers and lakes severe depletion of oxygen eutrophication, coastal waters red tide;Rubbish during corruption, Produce a large amount of heat energy, mainly ammonia, the pernicious gas such as methane and hydrogen sulfide, excessive concentration carries out stench, severe contamination air, Heat is distributed, city is surrounded from aerial, rubbish will spontaneous combustion, self-destruction phenomenon;Polybag, plastic cup and foam plastic product etc. White pollution is not easily decomposed, and is not only reduced city look and feel, environmental sanitation level, is lured harmful animal, have an effect on soil texture, Cause soil to deteriorate, contain crop growth, make the plant underproduction;Hazardous waste is directly or indirectly detrimental to health, such as useless lamp Pipe, particularly waste oil paint, refuse battery, because containing heavy metal substances such as mercury, cadmium and lead in battery, mercury has strong toxicity, Lead can cause neurological disorders, ephritis etc., and cadmium mainly causes kidney, hepatic injury and bone disease-osteoporosis, rickets and fracture, put Penetrating property can be carcinogenic.
Therefore, it is necessary to study a kind of processing method of municipal refuse, the danger of municipal refuse can be farthest reduced Evil.
The content of the invention
Not enough in order to overcome present in background technology, the present invention proposes a kind of processing method of municipal refuse, can be by The organic matter that can ferment carries out degradation treatment, and factor of created gase is higher, and resource utilization is high.
The present invention is achieved through the following technical solutions:
A kind of processing method of municipal refuse, comprises the following steps:
1) sort
Municipal refuse raw material is fed through in separator, can ferment organic matter and the inanimate matter that can not ferment is sub-elected;
2) crush
By the organic matter crusher in crushing of fermenting sub-elected;
3) ferment
Will it is broken after the organic matter that ferments add in fermentation tank, and add zymotic fluid, lipase and cellulase, It is 50-65 DEG C to control fermentation temperature, and pH is 6-8, and ferment 40-50h;
4) product is handled
The biogas that fermentation is produced is transported to biogas center, and biogas slurry and biogas residue are discharged after being post-processed.
Further, the particle diameter of crusher in crushing is 500-800 mesh.
Further, step 3) in, described zymotic fluid is acetic acid and the mixture of hydrochloric acid.
Further, the mass concentration of described acetic acid is 30-35%.
Further, the mass concentration of described hydrochloric acid is 40-45%.
Further, the volume ratio of described hydrochloric acid and acetic acid is 1-3:1.
Further, step 3) in, the volume ratio of described zymotic fluid, lipase and cellulase is 3-4:2-3:1.
Further, when handling degradable organic matter, zymotic fluid, lipase and cellulase weight sum are rubbish weight The 10-12% of amount.
Compared with prior art, the present invention at least has one of the following advantages:
1. municipal refuse is sorted, degradable organic matter can be handled by degrading, non-degradable inanimate matter Handled by other means again, it is to avoid municipal refuse is directly handled without sorting and handles incomplete drawback.
2. adding zymotic fluid, lipase and cellulase during the fermentation, the same of municipal refuse degraded is enabled to When, leaf brought into etc. is also degraded well;
3. the present invention is defined to the additional proportion of zymotic fluid, lipase and cellulase, enabling to ferment has The degradation rate of machine matter is higher, and factor of created gase is high so that municipal refuse is turned waste into wealth, and resource utilization is high.
Embodiment
In order that the purpose of the present invention, technical scheme and beneficial effect are clearer, the present invention is preferable to carry out below Example is described in detail, to facilitate the technical staff to understand.
Embodiment 1
A kind of processing method of municipal refuse, comprises the following steps:
1) sort
Municipal refuse raw material is fed through in separator, can ferment organic matter and the inanimate matter that can not ferment is sub-elected;
2) crush
By the organic matter crusher in crushing of fermenting sub-elected, the particle diameter of crusher in crushing is 500 mesh;
3) ferment
Will it is broken after the organic matter that ferments add in fermentation tank, and add zymotic fluid, lipase and cellulase, It is 50 DEG C to control fermentation temperature, and pH is 6, and ferment 40h, and zymotic fluid is the mixture of acetic acid and hydrochloric acid, and the mass concentration of acetic acid is 30%, the mass concentration of hydrochloric acid is 40%, and the volume ratio of hydrochloric acid and acetic acid is 1:1, and zymotic fluid, lipase and cellulose The volume ratio of enzyme is 3:2:1, when handling degradable organic matter, zymotic fluid, lipase and cellulase weight sum are rubbish The 10% of weight.
4) product is handled
The biogas that fermentation is produced is transported to biogas center, and biogas slurry and biogas residue are discharged after being post-processed.
Embodiment 2
A kind of processing method of municipal refuse, comprises the following steps:
1) sort
Municipal refuse raw material is fed through in separator, can ferment organic matter and the inanimate matter that can not ferment is sub-elected;
2) crush
By the organic matter crusher in crushing of fermenting sub-elected, the particle diameter of crusher in crushing is 650 mesh;
3) ferment
Will it is broken after the organic matter that ferments add in fermentation tank, and add zymotic fluid, lipase and cellulase, It is 55 DEG C to control fermentation temperature, and pH is 7, and ferment 45h, and zymotic fluid is the mixture of acetic acid and hydrochloric acid, and the mass concentration of acetic acid is 33%, the mass concentration of hydrochloric acid is 43%, and the volume ratio of hydrochloric acid and acetic acid is 2:1, and zymotic fluid, lipase and cellulose The volume ratio of enzyme is 3:2:1, when handling degradable organic matter, zymotic fluid, lipase and cellulase weight sum are rubbish The 11% of weight.
4) product is handled
The biogas that fermentation is produced is transported to biogas center, and biogas slurry and biogas residue are discharged after being post-processed.
Embodiment 3
A kind of processing method of municipal refuse, comprises the following steps:
1) sort
Municipal refuse raw material is fed through in separator, can ferment organic matter and the inanimate matter that can not ferment is sub-elected;
2) crush
By the organic matter crusher in crushing of fermenting sub-elected, the particle diameter of crusher in crushing is 800 mesh;
3) ferment
Will it is broken after the organic matter that ferments add in fermentation tank, and add zymotic fluid, lipase and cellulase, It is 65 DEG C to control fermentation temperature, and pH is 8, and ferment 50h, and zymotic fluid is the mixture of acetic acid and hydrochloric acid, and the mass concentration of acetic acid is 35%, the mass concentration of hydrochloric acid is 45%, and the volume ratio of hydrochloric acid and acetic acid is 3:1, and zymotic fluid, lipase and cellulose The volume ratio of enzyme is 4:3:1, when handling degradable organic matter, zymotic fluid, lipase and cellulase weight sum are rubbish The 12% of weight.
4) product is handled
The biogas that fermentation is produced is transported to biogas center, and biogas slurry and biogas residue are discharged after being post-processed.
Experimental analysis:
1. analyze degradation rate of the inventive method to degradable organic matter
1) experimental subjects
1 ton of degradable organic matter in municipal refuse.
2) experimental method
Take same place to carry out the mixed organic matter that ferments respectively, 3 tons, be divided into 3 parts and tested, be respectively real Group 1, experimental group 2 and experimental group 3 are tested, experimental group 1 is handled with the method for embodiment 1, experimental group is handled with the method for embodiment 2 2, handle experimental group 3 with the method for embodiment 3.
3) experimental result
The amount of the biogas to being produced in experimentation is measured respectively, and weighs the quality of last biogas residue, to result Counted, statistical result is as shown in table 1:
Table 1 can ferment organic matter degradation statistics
As can be seen from Table 1, the degradation rate of the of the invention pair of organic matter that can ferment is high, and gas production is big, can become municipal refuse Waste be changed into values, and comprehensive utilization ratio is high.
The present invention municipal refuse is sorted, degradable organic matter can be handled by degrading, non-degradable without Machine matter is handled by other means again, it is to avoid municipal refuse is directly handled without sorting and handles incomplete Drawback;Zymotic fluid, lipase and cellulase are added during the fermentation, while enabling to the municipal refuse to degrade, by band Leaf entered etc. is also degraded well;The present invention is limited the additional proportion of zymotic fluid, lipase and cellulase Fixed, the degradation rate for the organic matter that enables to ferment is higher, and factor of created gase is high so that municipal refuse is turned waste into wealth, resource utilization It is high.
Finally illustrate, preferred embodiment above is merely illustrative of the technical solution of the present invention and unrestricted, although logical Cross above preferred embodiment the present invention is described in detail, it is to be understood by those skilled in the art that can be Various changes are made to it in form and in details, without departing from claims of the present invention limited range.

Claims (8)

1. a kind of processing method of municipal refuse, it is characterised in that:Comprise the following steps:
1) sort
Municipal refuse raw material is fed through in separator, can ferment organic matter and the inanimate matter that can not ferment is sub-elected;
2) crush
By the organic matter crusher in crushing of fermenting sub-elected;
3) ferment
The organic matter that ferments after will be broken is added in fermentation tank, and adds zymotic fluid, lipase and cellulase, control hair Ferment temperature is 50-65 DEG C, and pH is 6-8, and ferment 40-50h;
4) product is handled
The biogas that fermentation is produced is transported to biogas center, and biogas slurry and biogas residue are discharged after being post-processed.
2. a kind of processing method of municipal refuse according to claim 1, it is characterised in that:Step 2) in, disintegrating machine is broken Broken particle diameter is 500-800 mesh.
3. a kind of processing method of municipal refuse according to claim 1, it is characterised in that:Step 3) in, described hair Zymotic fluid is the mixture of acetic acid and hydrochloric acid.
4. a kind of processing method of municipal refuse according to claim 3, it is characterised in that:The quality of described acetic acid is dense Spend for 30-35%.
5. a kind of processing method of municipal refuse according to claim 3, it is characterised in that:The quality of described hydrochloric acid is dense Spend for 40-45%.
6. a kind of processing method of municipal refuse according to claim 3, it is characterised in that:Described hydrochloric acid and acetic acid Volume ratio is 1-3:1.
7. a kind of processing method of municipal refuse according to claim 1, it is characterised in that:Step 3) in, described hair The volume ratio of zymotic fluid, lipase and cellulase is 3-4:2-3:1.
8. a kind of processing method of municipal refuse according to claim 1, it is characterised in that:In processing degradable organic matter When, zymotic fluid, lipase and cellulase weight sum are the 10-12% of garbage weight.
CN201710295388.6A 2017-04-28 2017-04-28 A kind of processing method of municipal refuse Pending CN107142283A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710295388.6A CN107142283A (en) 2017-04-28 2017-04-28 A kind of processing method of municipal refuse

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710295388.6A CN107142283A (en) 2017-04-28 2017-04-28 A kind of processing method of municipal refuse

Publications (1)

Publication Number Publication Date
CN107142283A true CN107142283A (en) 2017-09-08

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101993813A (en) * 2009-08-18 2011-03-30 包德圻 Method for realizing energy biogasification by using waste biology
CN103272829A (en) * 2013-06-03 2013-09-04 邓锦新 Urban living garbage treatment method
CN106399386A (en) * 2016-12-02 2017-02-15 中科院广州能源所盱眙凹土研发中心 Method for producing biological fuel gas by using fruit and vegetable garbage
CN106513414A (en) * 2016-10-31 2017-03-22 南开大学 Process technology for fully recycling municipal domestic waste and producing engineering raw materials from municipal domestic waste and application

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101993813A (en) * 2009-08-18 2011-03-30 包德圻 Method for realizing energy biogasification by using waste biology
CN103272829A (en) * 2013-06-03 2013-09-04 邓锦新 Urban living garbage treatment method
CN106513414A (en) * 2016-10-31 2017-03-22 南开大学 Process technology for fully recycling municipal domestic waste and producing engineering raw materials from municipal domestic waste and application
CN106399386A (en) * 2016-12-02 2017-02-15 中科院广州能源所盱眙凹土研发中心 Method for producing biological fuel gas by using fruit and vegetable garbage

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
TAHERZADEH MJ等: "Pretreatment of lignocellulosic wastes to improve ethanol and biogas production: a review", 《INT J MOL SCI.》 *
李炎: "《生物再生能源技术》", 31 January 2013 *
甘福丁: "《规模化禽畜养殖场沼气工程》", 30 June 2016, 广西科学技术出版社 *

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Application publication date: 20170908