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CN106122968A - Preprocess method before one way of life waste incineration - Google Patents

Preprocess method before one way of life waste incineration Download PDF

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Publication number
CN106122968A
CN106122968A CN201610471878.2A CN201610471878A CN106122968A CN 106122968 A CN106122968 A CN 106122968A CN 201610471878 A CN201610471878 A CN 201610471878A CN 106122968 A CN106122968 A CN 106122968A
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China
Prior art keywords
refuse
organic waste
waste
fertilizer
preprocess method
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Pending
Application number
CN201610471878.2A
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Chinese (zh)
Inventor
吴任枝
谢胜
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Science And Technology Development Centre Pubei County
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Science And Technology Development Centre Pubei County
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.)
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Application filed by Science And Technology Development Centre Pubei County filed Critical Science And Technology Development Centre Pubei County
Priority to CN201610471878.2A priority Critical patent/CN106122968A/en
Publication of CN106122968A publication Critical patent/CN106122968A/en
Pending legal-status Critical Current

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/20Agglomeration, binding or encapsulation of solid waste
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F3/00Fertilisers from human or animal excrements, e.g. manure
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05GMIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
    • C05G3/00Mixtures of one or more fertilisers with additives not having a specially fertilising activity
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/033Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment comminuting or crushing
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00Pretreatment
    • F23G2201/60Separating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00Pretreatment
    • F23G2201/60Separating
    • F23G2201/603Separating recyclable material
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00Pretreatment
    • F23G2201/70Blending
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00Pretreatment
    • F23G2201/70Blending
    • F23G2201/701Blending with additives
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00Pretreatment
    • F23G2201/80Shredding
    • 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
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Pest Control & Pesticides (AREA)
  • Environmental & Geological Engineering (AREA)
  • Biochemistry (AREA)
  • Biotechnology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • Molecular Biology (AREA)
  • Fertilizers (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The invention belongs to technical field of waste treatment, the specifically preprocess method before one way of life waste incineration, step is as follows: carry out house refuse tearing up, after broken bag processes, filter out metallics and reclaim sale, remaining refuse classification is organic waste and inorganic refuse, organic waste is used for making fertilizer after harmless treatment, for burning electricity generation after mixing with coal grain after inorganic refuse pulverizing.Categorized consumer waste is recoverable metal, inorganic refuse and organic waste several types by the method for the present invention by categorized consumer waste, and then use different processing modes, metallics can be recycled, the fertilizer that fertilizer efficiency is good can also be prepared, being applied individually to burn additionally due to isolated inorganic refuse, the calorific value of burning is higher, it is less to burn the pollutant produced.

Description

Preprocess method before one way of life waste incineration
Technical field
The present invention relates to technical field of waste treatment, having is the preprocess method before one way of life waste incineration.
Background technology
Trash processing way can be generally divided into the several ways such as health burning, burning, compost.Waste incineration, or claim rubbish Rubbish incinerates, and is the method for a kind of refuse process, by organic substance in incinerating waste material, to reduce Waste volume.Burn and other High temperature refuse disposal system, is all referred to as " heat treatment ".Can convert garbage into as ashes, waste gas and heating power when incinerating rubbish.Ash Cinder is made up of the inorganic substances in refuse mostly, generally presents with forms such as the microgranules in solid and waste gas.Waste gas is being discharged into Before in air, needing to remove wherein dusty gas and microgranule, remaining residue is then for landfill.In some situation, incinerate rubbish Heat energy produced by rubbish can be used for generating electricity, heating.But waste incineration also has operating cost high, and incinerating combustion value is low, takes in waste gas Carry the shortcomings such as a large amount of pollutant.So carrying out rational pretreatment before waste incineration, it is possible to effectively reduce its harm and reduce Burn cost.
Summary of the invention
The technical problem to be solved in the present invention is to provide the preprocess method before one way of life waste incineration, to reduce rubbish Burn the harm produced.
For solve above-mentioned technical problem, the present invention by the following technical solutions:
Preprocess method before one way of life waste incineration, be carry out house refuse tearing up, after broken bag processes, screening Going out metallics and reclaim sale, remaining refuse classification is organic waste and inorganic refuse, and organic waste is after harmless treatment For making fertilizer, for burning electricity generation after mixing with coal grain after inorganic refuse pulverizing.
Further improvement as technique scheme:
The method of described screening is preferably electromagnetism screening.
The process that described harmless treatment processes is: is put into by organic waste in the water of its weight 2~3 times, regulates pH value Regulation is to 9~11, and continuous aeration processes 12~24 hours, is stirred continuously organic waste, then filters in aeration process, and filtering residue is used In making fertilizer, filtrate puts into the heavy metal scavenger of its weight 0.1%~1%, under conditions of being stirred continuously react 30~ 60min, is subsequently adding flocculant flocculation sediment, and gained supernatant is reused for carrying out mixed processing with new organic waste.
Wherein, the preparation process of described heavy metal scavenger is: add iron chloride, aluminum chloride and manganese chloride, system in water Iron concentration be 0.5~1mol/L, aluminium ion concentration be 0.8~1.2mol/L, manganese ion concentration be 0.1~0.5mol/L Mixed solution, in the case of being stirred continuously, add sodium hydroxide solution regulation to pH value be 7~8, stand clarification after take heavy Form sediment, after washing precipitate 3~5 times with water, be dried and be crushed to 80~120 mesh,.
Described make fertilizer process be: by gained filtering residue, agricultural crop straw and cattle manure mixing pile 100~150 centimetres High stockpile, spreads last layer Testa oryzae, then overlay film at stockpile outer layer, and the temperature controlling fermentation is 60~70 DEG C, and carbon-nitrogen ratio is≤ 20, after fermenting 10~20 days, after mixing homogeneously, obtain fertilizer with copper sulfate;Filtering residue after deodorization process, agricultural crop straw, cattle The weight ratio of excrement, Testa oryzae and copper sulfate is 30~50:50~80:10~30:5~15:1~5.
Wherein, the weight ratio of filtering residue, agricultural crop straw, cattle manure, Testa oryzae and copper sulfate after described deodorization processes is preferably 40:65:20:12:3。
Described inorganic refuse mixes with the coal grain that particle diameter is 10~20mm after being ground into the granule of particle diameter 1~10mm, Inorganic refuse is 1:0.05~0.2 with the weight ratio of coal grain.
The invention have the benefit that
The method step of the present invention is simple and easy to control, is recoverable metal, inorganic refuse and organic rubbish by categorized consumer waste Rubbish several types, and then use different processing modes, metallics can be recycled, moreover it is possible to prepared heavy metal free pollution, The fertilizer that fertilizer efficiency is good, is applied individually to burn additionally due to isolated inorganic refuse, and the calorific value of burning is higher, burn generation Pollutant are less, it is possible to realize the recycling of house refuse and reduce the purpose burning harm.
Detailed description of the invention
Below in conjunction with specific embodiment for instruction and explanation of the present invention.
Embodiment 1
Preprocess method before one way of life waste incineration, carries out house refuse tearing up, after broken bag processes, filters out Metallics reclaims to be sold, and remaining refuse classification is organic waste and inorganic refuse, and organic waste is used after harmless treatment In making fertilizer, for burning electricity generation after mixing with coal grain after inorganic refuse pulverizing.
The process that described harmless treatment processes is: put into by organic waste in the water of its weight 2.5 times, and regulation pH value is adjusted Joint is to 10, and continuous aeration processes 18 hours, is stirred continuously organic waste, then filters in aeration process, and filtering residue is used for making fertilizer Material, filtrate puts into the heavy metal scavenger of its weight 0.5%, reacts 50min, be subsequently adding flocculation under conditions of being stirred continuously Agent flocculation sediment, gained supernatant is reused for carrying out mixed processing with new organic waste.
Wherein, the preparation process of described heavy metal scavenger is: add iron chloride, aluminum chloride and manganese chloride, system in water Iron concentration be 0.8mol/L, aluminium ion concentration be 0.9mol/L, manganese ion concentration be the mixed solution of 0.4mol/L, In the case of being stirred continuously, adding sodium hydroxide solution regulation is 8 to pH value, takes precipitation, wash precipitation with water after standing clarification After thing 4 times, it is dried and is crushed to 100 mesh,.
Described make fertilizer process be: by gained filtering residue, agricultural crop straw and cattle manure mixing pile 100~150 centimetres High stockpile, spreads last layer Testa oryzae, then overlay film at stockpile outer layer, and the temperature controlling fermentation is 60~70 DEG C, and carbon-nitrogen ratio is≤ 20, after fermenting 15 days, after mixing homogeneously, obtain fertilizer with copper sulfate;Filtering residue after deodorization process, agricultural crop straw, cattle manure, rice The weight ratio of bran and copper sulfate is 40:65:20:12:3.
Described inorganic refuse mixes with the coal grain that particle diameter is 10~20mm after being ground into the granule of particle diameter 1~10mm, Inorganic refuse is 1:0.1 with the weight ratio of coal grain.
Embodiment 2
Preprocess method before one way of life waste incineration, carries out house refuse tearing up, after broken bag processes, filters out Metallics reclaims to be sold, and remaining refuse classification is organic waste and inorganic refuse, and organic waste is used after harmless treatment In making fertilizer, for burning electricity generation after mixing with coal grain after inorganic refuse pulverizing.
The process that described harmless treatment processes is: put into by organic waste in the water of its weight 2 times, regulation pH value regulation To 9, continuous aeration processes 24 hours, is stirred continuously organic waste, then filters in aeration process, and filtering residue is used for making fertilizer, Filtrate puts into the heavy metal scavenger of its weight 1%, reacts 30min under conditions of being stirred continuously, and is subsequently adding flocculant wadding Retrogradation is formed sediment, and gained supernatant is reused for carrying out mixed processing with new organic waste.
Wherein, the preparation process of described heavy metal scavenger is: add iron chloride, aluminum chloride and manganese chloride, system in water Iron concentration be 0.5mol/L, aluminium ion concentration be 1.2mol/L, manganese ion concentration be the mixed solution of 0.5mol/L, In the case of being stirred continuously, adding sodium hydroxide solution regulation is 7 to pH value, takes precipitation, wash precipitation with water after standing clarification After thing 3 times, it is dried and is crushed to 120 mesh,.
Described make fertilizer process be: by gained filtering residue, agricultural crop straw and cattle manure mixing pile 100~150 centimetres High stockpile, spreads last layer Testa oryzae, then overlay film at stockpile outer layer, and the temperature controlling fermentation is 60~70 DEG C, and carbon-nitrogen ratio is≤ 20, after fermenting 20 days, after mixing homogeneously, obtain fertilizer with copper sulfate;Filtering residue after deodorization process, agricultural crop straw, cattle manure, rice The weight ratio of bran and copper sulfate is 30:50:30:15:1.
Described inorganic refuse mixes with the coal grain that particle diameter is 10~20mm after being ground into the granule of particle diameter 1~10mm, Inorganic refuse is 1:0.05 with the weight ratio of coal grain.
Embodiment 3
Preprocess method before one way of life waste incineration, carries out house refuse tearing up, after broken bag processes, filters out Metallics reclaims to be sold, and remaining refuse classification is organic waste and inorganic refuse, and organic waste is used after harmless treatment In making fertilizer, for burning electricity generation after mixing with coal grain after inorganic refuse pulverizing.
The process that described harmless treatment processes is: put into by organic waste in the water of its weight 3 times, regulation pH value regulation To 11, continuous aeration processes 12 hours, is stirred continuously organic waste, then filters in aeration process, and filtering residue is used for making fertilizer, Filtrate puts into the heavy metal scavenger of its weight 0.1%, reacts 60min, be subsequently adding flocculant under conditions of being stirred continuously Flocculation sediment, gained supernatant is reused for carrying out mixed processing with new organic waste.
Wherein, the preparation process of described heavy metal scavenger is: add iron chloride, aluminum chloride and manganese chloride, system in water Iron concentration be 1mol/L, aluminium ion concentration be 0.8mol/L, manganese ion concentration be the mixed solution of 0.1mol/L, not In the case of disconnected stirring, adding sodium hydroxide solution regulation is 8 to pH value, takes precipitation, wash precipitate 5 with water after standing clarification After secondary, it be dried and be crushed to 80 mesh,.
Described make fertilizer process be: by gained filtering residue, agricultural crop straw and cattle manure mixing pile 100~150 centimetres High stockpile, spreads last layer Testa oryzae, then overlay film at stockpile outer layer, and the temperature controlling fermentation is 60~70 DEG C, and carbon-nitrogen ratio is≤ 20, after fermenting 10 days, after mixing homogeneously, obtain fertilizer with copper sulfate;Filtering residue after deodorization process, agricultural crop straw, cattle manure, rice The weight ratio of bran and copper sulfate is 50:80:10:5:5.
Described inorganic refuse mixes with the coal grain that particle diameter is 10~20mm after being ground into the granule of particle diameter 1~10mm, Inorganic refuse is 1:0.2 with the weight ratio of coal grain.

Claims (6)

1. the preprocess method before one way of life waste incineration, it is characterised in that carry out house refuse tearing up, broken bag processes it After, filtering out metallics and reclaim sale, remaining refuse classification is organic waste and inorganic refuse, and organic waste is through innoxious It is used for making fertilizer after process, for burning electricity generation after mixing with coal grain after inorganic refuse pulverizing.
Preprocess method the most according to claim 1, it is characterised in that the method for described screening is electromagnetism screening.
Preprocess method the most according to claim 1, it is characterised in that the process that described harmless treatment processes is: will Organic waste puts in the water of its weight 2~3 times, and regulation pH value regulates to 9~11, and continuous aeration processes 12~24 hours, exposes Being stirred continuously organic waste during gas, then filter, filtering residue is used for making fertilizer, and filtrate puts into its weight 0.1%~1% Heavy metal scavenger, reacts 30~60min under conditions of being stirred continuously, is subsequently adding flocculant flocculation sediment, gained supernatant Liquid is reused for carrying out mixed processing with new organic waste;
The preparation process of described heavy metal scavenger is: adds iron chloride, aluminum chloride and manganese chloride in water, prepares iron ion dense Degree is 0.5~1mol/L, aluminium ion concentration is 0.8~1.2mol/L, manganese ion concentration be 0.1~0.5mol/L mixing molten Liquid, in the case of being stirred continuously, adding sodium hydroxide solution regulation is 7~8 to pH value, takes precipitation, use water after standing clarification After washing precipitate 3~5 times, it is dried and is crushed to 80~120 mesh,.
Preprocess method the most according to claim 3, it is characterised in that described in make the process of fertilizer and be: gained is filtered Slag, agricultural crop straw and cattle manure mixing pile 100~150 centimetres of high stockpiles, spread last layer Testa oryzae at stockpile outer layer, then cover Film, the temperature controlling fermentation is 60~70 DEG C, and carbon-nitrogen ratio is≤20, after fermenting 10~20 days, after mixing homogeneously with copper sulfate To fertilizer;The weight ratio of filtering residue, agricultural crop straw, cattle manure, Testa oryzae and copper sulfate after deodorization process is 30~50:50~80: 10~30:5~15:1~5.
Preprocess method the most according to claim 4, it is characterised in that: the filtering residue after described deodorization process, crops straw The weight ratio of stalk, cattle manure, Testa oryzae and copper sulfate is 40:65:20:12:3.
Preprocess method the most according to claim 1, it is characterised in that: described inorganic refuse is ground into particle diameter 1~10mm Granule after mix with the coal grain that particle diameter is 10~20mm, the weight ratio of inorganic refuse and coal grain is 1:0.05~0.2.
CN201610471878.2A 2016-06-24 2016-06-24 Preprocess method before one way of life waste incineration Pending CN106122968A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106824984A (en) * 2017-01-12 2017-06-13 湖南万容科技股份有限公司 A kind of life refuse processing method
CN108114968A (en) * 2017-12-21 2018-06-05 杨恒武 A kind of garbage classification processing method

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1177525A (en) * 1996-09-23 1998-04-01 中国科学院成都生物研究所 Process for treatment of organic garbage of city
CN1442242A (en) * 2002-09-19 2003-09-17 齐继红 City life garbage fast and harmless comprehensive treatment method
CN1857805A (en) * 2006-06-03 2006-11-08 薛占何 Garbage treating and utilizing process for small town
CN101683653A (en) * 2008-09-26 2010-03-31 张学法 Municipal refuse treatment method
CN102583313A (en) * 2012-02-14 2012-07-18 浙江大学 Rural household garbage carbonization method, prepared products using same, and application
CN102701711A (en) * 2012-06-27 2012-10-03 刘梁 Sintered brick and manufacturing method thereof
CN104446179A (en) * 2014-11-04 2015-03-25 临沂清宇环境资源工程设备有限公司 Method for manufacturing hollow brick by using non-recyclable waste
CN104591691A (en) * 2013-10-30 2015-05-06 徐小芹 Technology for firing common bricks from fresh municipal domestic waste
CN104801528A (en) * 2014-01-28 2015-07-29 常州大学 Domestic waste organic treatment method
CN105084865A (en) * 2014-05-08 2015-11-25 闵建华 Process for sintering common bricks by using fresh municipal domestic waste

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1177525A (en) * 1996-09-23 1998-04-01 中国科学院成都生物研究所 Process for treatment of organic garbage of city
CN1442242A (en) * 2002-09-19 2003-09-17 齐继红 City life garbage fast and harmless comprehensive treatment method
CN1857805A (en) * 2006-06-03 2006-11-08 薛占何 Garbage treating and utilizing process for small town
CN101683653A (en) * 2008-09-26 2010-03-31 张学法 Municipal refuse treatment method
CN102583313A (en) * 2012-02-14 2012-07-18 浙江大学 Rural household garbage carbonization method, prepared products using same, and application
CN102701711A (en) * 2012-06-27 2012-10-03 刘梁 Sintered brick and manufacturing method thereof
CN104591691A (en) * 2013-10-30 2015-05-06 徐小芹 Technology for firing common bricks from fresh municipal domestic waste
CN104801528A (en) * 2014-01-28 2015-07-29 常州大学 Domestic waste organic treatment method
CN105084865A (en) * 2014-05-08 2015-11-25 闵建华 Process for sintering common bricks by using fresh municipal domestic waste
CN104446179A (en) * 2014-11-04 2015-03-25 临沂清宇环境资源工程设备有限公司 Method for manufacturing hollow brick by using non-recyclable waste

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106824984A (en) * 2017-01-12 2017-06-13 湖南万容科技股份有限公司 A kind of life refuse processing method
CN108114968A (en) * 2017-12-21 2018-06-05 杨恒武 A kind of garbage classification processing method

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Application publication date: 20161116