CN105689356A - Process for making biomass fuel by mixing municipal domestic garbage with industrial organic garbage - Google Patents
Process for making biomass fuel by mixing municipal domestic garbage with industrial organic garbage Download PDFInfo
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- CN105689356A CN105689356A CN201410694992.2A CN201410694992A CN105689356A CN 105689356 A CN105689356 A CN 105689356A CN 201410694992 A CN201410694992 A CN 201410694992A CN 105689356 A CN105689356 A CN 105689356A
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- class rubbish
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- organic waste
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- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 63
- 238000000034 method Methods 0.000 title claims abstract description 62
- 230000008569 process Effects 0.000 title claims abstract description 43
- 239000000446 fuel Substances 0.000 title claims abstract description 22
- 238000002156 mixing Methods 0.000 title claims abstract description 19
- 239000002028 Biomass Substances 0.000 title claims abstract description 15
- 239000003205 fragrance Substances 0.000 claims abstract description 5
- 241000894006 Bacteria Species 0.000 claims abstract description 4
- 238000000855 fermentation Methods 0.000 claims abstract description 4
- 230000004151 fermentation Effects 0.000 claims abstract description 4
- 238000006303 photolysis reaction Methods 0.000 claims abstract description 4
- 239000010815 organic waste Substances 0.000 claims description 25
- 238000001035 drying Methods 0.000 claims description 13
- 239000010791 domestic waste Substances 0.000 claims description 12
- 238000000746 purification Methods 0.000 claims description 11
- 239000002781 deodorant agent Substances 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 238000002485 combustion reaction Methods 0.000 claims description 4
- 238000001125 extrusion Methods 0.000 claims description 4
- 238000005469 granulation Methods 0.000 claims description 4
- 230000003179 granulation Effects 0.000 claims description 4
- 239000002304 perfume Substances 0.000 claims description 4
- 239000002154 agricultural waste Substances 0.000 claims description 3
- 238000011109 contamination Methods 0.000 claims description 3
- 238000005065 mining Methods 0.000 claims description 3
- 239000007921 spray Substances 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 239000000758 substrate Substances 0.000 claims description 3
- 230000001877 deodorizing effect Effects 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 7
- 239000002245 particle Substances 0.000 abstract description 6
- 238000004332 deodorization Methods 0.000 abstract description 5
- 238000003912 environmental pollution Methods 0.000 abstract description 4
- 125000003118 aryl group Chemical group 0.000 abstract description 2
- 230000008901 benefit Effects 0.000 abstract description 2
- 238000005265 energy consumption Methods 0.000 abstract description 2
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 230000015843 photosynthesis, light reaction Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 11
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 239000010865 sewage Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 230000000844 anti-bacterial effect Effects 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000002912 waste gas Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 101001031591 Mus musculus Heart- and neural crest derivatives-expressed protein 2 Proteins 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- WQOXQRCZOLPYPM-UHFFFAOYSA-N dimethyl disulfide Chemical compound CSSC WQOXQRCZOLPYPM-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 2
- -1 sulfur hydrogen Chemical class 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 1
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- CKUAXEQHGKSLHN-UHFFFAOYSA-N [C].[N] Chemical compound [C].[N] CKUAXEQHGKSLHN-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000002551 biofuel Substances 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000007523 nucleic acids Chemical class 0.000 description 1
- 102000039446 nucleic acids Human genes 0.000 description 1
- 108020004707 nucleic acids Proteins 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000006385 ozonation reaction Methods 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
-
- 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
Abstract
The invention discloses a process for making biomass fuel by mixing municipal domestic garbage with industrial organic garbage, realizes reuse of domestic garbage and industrial garbage, and makes biomass fuel particles. At the same time, by means of energy supply in the process, the whole process has the advantages of low energy consumption and no environmental pollution. In addition, deodorization measures involved in the process include EM bacteria liquid pretreatment fermentation deodorization and photolysis of malodorous gas. The process provided by the invention not only increases the deodorization treatment in a working environment, prevents stinking water and stench leakage to harm the surrounding environment and cause resident objection, at the same times adds product deodorization treatment, so that the made fuel particles is free of odor. A more advanced point lies that a perfuming program is added, and a natural aromatic (fragrance optional) can be added in the environment and product according to needs, so that the working environment and the product can both have slight natural plant fragrance.
Description
Technical field
The present invention relates to technical field of new energies, particularly to a kind of technique that domestic waste and industry organic waste mixing are manufactured biomass fuel。
Background technology
Along with growth in the living standard, the house refuse that the mankind produce gets more and more, simultaneously because the industrial industrial refuse needing to produce also day by day increases, traditional mode processing rubbish mainly has landfill, burning, but environment can be caused secondary pollution by this both of which, it is also generally it is carried out cutting classification process take its useful part that present so-called garbage reclamation utilizes, and such as metal, plastics etc., both is the problem fundamentally solving environmental pollution and garbage reclamation utilization。The patent application that China's application number is 2201210178678.X discloses a kind of technique utilizing biologic garbage to manufacture bio-fuel, first biologic garbage is carried out water squeezing processing, biologic garbage after water squeezing is divided into two classes and processes simultaneously, the sewage of the first kind produces biogas, the heat energy of biogas combustion is as drying heat energy, and the block biologic garbage of Equations of The Second Kind carries out chopping process；Biologic garbage after chopping delivers into drying plant and dries；The waste gas that drying plant is discharged sequentially passes through qualified discharge after primary purification equipment, double purification equipment, and it is finished product that the biologic garbage after drying delivers into Granulation Equipments pelletize。
Present invention be distinguished in that: one is the harmful gas overcoming the generation of the aforementioned Chinese patent technical finesse process pollution to environment；Two is make environment and product all have the fragrant breath of natural plants by increase natural perfume material, makes people happy；Three is that foregoing invention patent mainly processes biologic garbage, is not particularly suited for life and industrial refuse, and house refuse and industry organic waste proportioning by a certain percentage are processed and make biomass fuel pellet by the present invention。
Summary of the invention
The technical problem to be solved is to provide one by domestic waste and industry organic waste mixed processing, and can carry out the technique mixing the fuel particle manufacturing different calorific value of stink process。
In order to realize the purpose of the present invention, technical scheme provided by the invention: a kind of technique that domestic waste and industry organic waste mixing are manufactured biomass fuel, comprise the steps:
1. spray low concentration EM bacterium solution during garbage sorting, carry out fermentation deodorant and process。House refuse after sorting is divided into A class and B class process, and described A class rubbish thing moisture is not less than 70%, and described B class rubbish thing moisture is lower than 70%；
2. A class rubbish thing being carried out mechanical presses moisture, the moisture of extrusion puts into seal of vessel, and the A class rubbish after extruding is put into drying plant；
3. container is placed 5-10 days at 40-45 DEG C of constant temperature lower seal；
4. the biogas produced in container pass into combustion furnace burning, and its heat energy is sent to drying plant, thus being reduced further by the A class refuse moisture after extruding。
5. by B class rubbish through mechanical presses, moisture road after primary purification device processes is sent into the stink of primary purification processor and is processed equipment, and another road is sent into the stink of secondary purifier and processed equipment, and stink processes after equipment internal contamination substrate concentration raises and sends in container。
6. after the A class rubbish after drying and the B class rubbish mixing after chopping, add industrial refuse, three is mixed and after smashing and add natural perfume material, sends into Granulation Equipments。
Preferably, described container is march gas producing container。
Preferably, the stink in described primary purification device and secondary purifier processes equipment and is photodissociation foul gas depurator。
Preferably, described industrial refuse is mining industry solid organic waste substances, industrial solid organic waste or agricultural wastes。
Preferably, described step 5. in, A class rubbish, B class rubbish and industry organic waste mass ratio be 4:2:4。
Preferably, described step 5. in, A class rubbish, B class rubbish and industry organic waste mass ratio be 5:2:3。
Preferably, described step 5. in, A class rubbish, B class rubbish and industry organic waste mass ratio be 4:1:5。
Beneficial effects of the present invention: the present invention achieves the recycling of house refuse and industrial refuse by above-mentioned technological process, produces dye granule, and present invention process is by energy supply in technique simultaneously, and whole technique has the advantage that energy consumption is low, free from environmental pollution；The stink additionally increased in the depurator of this technique processes equipment, and the deodorant increasing working environment processes, it is prevented that smelly water, foul smell leak, endanger surrounding, cause resident to oppose, the deodorant simultaneously increasing product processes, and makes the fuel particle produced be destitute of smell, does not result in odor pollution。More advanced is set up perfuming program, can as needed in adding natural aromatic agent (fragrance is optional) in environment and product so that working environment and product all have light natural plants fragrance breath。
Accompanying drawing explanation
Fig. 1 is the process chart of the present invention。
Detailed description of the invention
Embodiment 1:As it is shown in figure 1, a kind of technique that domestic waste and industry organic waste mixing are manufactured biomass fuel, comprise the steps:
1. spray low concentration EM bacterium solution during garbage sorting, carry out fermentation deodorant and process。House refuse after sorting 1 is divided into A class 2 and B class 3 process, and described A class rubbish thing 2 moisture is not less than 70%, and house refuse, lower than 70%, is namely carried out classification process according to moisture in refuse classification guiding and garbage reclamation stage by described B class 3 rubbish thing moisture。
2. A class rubbish thing 2 being carried out mechanical presses moisture, can adopt drum extrusion or flat board pressure filtering technique, the moisture 7 of extrusion is put into container 8 and is sealed, then the A class rubbish 5 after extruding is put into drying plant 6。
3. container 8 is placed 5-10 days at 40-45 DEG C of constant temperature lower seal, owing to the moisture 7 after extruding containing sufficient strain, CH4The temperature, concentration, acid-base value, anaerobic environment and the carbon-nitrogen ratio that generate are all suitable, additionally can arrange mechanical type agitating device in container 8 and be stirred, in order to make full use of the biogas of remnants。
4. the biogas produced in container 8 is passed into combustion furnace burning by pipeline, utilize its heat energy to be sent to drying plant 6, thus A class rubbish 5 moisture after extruding is reduced further, it is not necessary to heat credit is thus saving energy, and the burning situation friendliness of biogas is high。
5. by B class rubbish 3 rubbish through mechanical presses, moisture 9 road after primary purification device 10 processes is sent into the stink of primary purification processor and is processed equipment 13, another road is sent into the stink of secondary purifier and is processed equipment 14, stink processes to be sent in container 8 after equipment 13,14 internal contamination substrate concentration raises, the depurator adopted in this technique all includes sewage disposal device, waste gas treatment equipment and stink and processes equipment 13,14, is provided with process pond (inside setting water) stink, abnormal flavour are neutralized in stink process equipment 13,14。Before sewage disposal device and waste gas treatment equipment are arranged at sewage and toxic emission technique, in order to make emission compliance, it is prevented that cause environmental pollution。One group of stink processes 13 equipment increases the deodorant process of working environment, it is prevented that smelly water, foul smell leak, and endanger surrounding, cause resident to oppose；Another group stink processes equipment 14 and processes producing product, makes the fuel particle produced be destitute of smell, and the client workman using fuel will not be caused to oppose。
6. after the A class rubbish after drying and the B class rubbish mixing after chopping, industrial organic waste 4 is added, the mass ratio of A class rubbish, B class rubbish and industry organic waste 4 is 4:2:4, Granulation Equipments 15 is sent into after three's mixing being smashed and add natural perfume material, owing to B class rubbish mostly is big bulk, in order to improve prilling, the B rubbish after extruding is carried out machinery chopping process 12, industry organic waste 4 is added house refuse 1, it is possible to promote the calorific value of fuel。
Embodiment 2:
All the other are identical with embodiment 1, it is different in that, container 8 adopts march gas producing container, stink in primary purification device and secondary purifier processes equipment and is photodissociation foul gas depurator, deodorization quadruple effect carries out simultaneously: one, special high energy high ozone UV ultraviolet beam is utilized to irradiate foul gas, change foul gas such as ammonia, trimethylamine, hydrogen sulfide, first sulfur hydrogen, methanthiol, methyl sulfide, methyl disulfide, Carbon bisulfide and styrene, sulfide H2S, VOC class, benzene, toluene, the molecular chain structure of dimethylbenzene, make organic or inorganic macromolecule malodorous compound strand, under high energy ultraviolet Line beam irradiates, degraded is transformed into low molecular compound, such as CO2, H2O etc.；Two, utilize high energy high ozone UV ultraviolet beam to decompose the oxygen molecule in air and produce free oxygen, i.e. active oxygen, because the taken positron-electron of free oxygen is uneven so need to be combined with oxygen molecule, and then generation ozone, UV+O2 → O-+O* (active oxygen) O+O2 → O3 (ozone), it is known that Pre-Ozonation on Organic Matter has extremely strong Oxidation, foul gas and other zest abnormal flavour there is the elimination effect got instant result；Three, after odour utilizes exhaust equipment to be input to this cleaning equipment, cleaning equipment uses high energy UV ultraviolet beam and ozone that foul gas carries out collaborative decomposition oxidation reaction, its Degradation and Transformation of foul gas material is made to become low molecular compound, water and carbon dioxide, outside again through exhaust duct discharge chamber；Four, utilize the molecular link of antibacterial in high energy UV light beam cracking foul gas, destroy the nucleic acid (DNA) of antibacterial, carry out oxidation reaction again through ozone, thoroughly reach deodorize and kill the purpose of antibacterial。
Additionally industry organic waste 4 can be mining industry solid organic waste substances, industrial solid debirs or agricultural wastes weight any one, owing to its calorific value of difference of industrial refuse kind is also different, thus need the fuel particle of the different calorific value of preparation according to different process。
Embodiment 3:All the other are identical with embodiment 1, are different in that, described step 5. in, the mass ratio of A class rubbish, B class rubbish and industrial refuse is 5:2:3。
Embodiment 4:All the other are identical with embodiment 1, are different in that, described step 5. in, the mass ratio of A class rubbish, B class rubbish and industrial refuse is 4:1:5。
Above-described is only the preferred embodiment of the present invention, it is noted that for the person of ordinary skill of the art, without departing from the concept of the premise of the invention, it is also possible to making some deformation and improvement, these broadly fall into protection scope of the present invention。
Claims (7)
1. the technique that domestic waste and industry organic waste mixing are manufactured biomass fuel, it is characterized in that, comprise the steps: 1. garbage sorting time spray low concentration EM bacterium solution, carry out fermentation deodorant to process, house refuse after sorting is divided into A class and B class process, described A class rubbish thing moisture is not less than 70%, and described B class rubbish thing moisture is lower than 70%；
2. A class rubbish thing being carried out mechanical presses moisture, the moisture of extrusion puts into seal of vessel, and the A class rubbish after extruding is put into drying plant；
3. container is placed 5-10 days at 40-45 DEG C of constant temperature lower seal；
4. the biogas produced in container pass into combustion furnace burning, and its heat energy is sent to drying plant, thus being reduced further by the A class refuse moisture after extruding；
5. by B class rubbish through mechanical presses, moisture road after primary purification device processes is sent into the stink of primary purification processor and is processed equipment, another road is sent into the stink of secondary purifier and is processed equipment, stink processes to be sent in container after equipment internal contamination substrate concentration raises, flavouring equipment is placed on deodorizing device side, gives out natural plant fragrance breath；
6. after the A class rubbish after drying and the B class rubbish mixing after chopping, add industrial organic waste, after three's mixing being smashed and add natural perfume material, send into Granulation Equipments。
2. a kind of technique that domestic waste and industry organic waste mixing are manufactured biomass fuel according to claim 1, it is characterised in that described container is march gas producing container。
3. a kind of technique that domestic waste and industry organic waste mixing are manufactured biomass fuel according to claim 1 and 2, it is characterised in that the stink in described primary purification device and secondary purifier processes equipment and is photodissociation foul gas depurator。
4. a kind of technique that domestic waste and industry organic waste mixing are manufactured biomass fuel according to claim 5, it is characterised in that described industrial refuse is mining industry solid organic waste substances, industrial solid debirs or agricultural wastes。
5. according to claim 4 a kind of by domestic waste and industry organic waste mixing manufacture biomass fuel technique, it is characterised in that described step 5. in, the mass ratio of A class rubbish, B class rubbish and industrial refuse is 4:2:4。
6. according to claim 4 a kind of by domestic waste and industry organic waste mixing manufacture biomass fuel technique, it is characterised in that described step 5. in, the mass ratio of A class rubbish, B class rubbish and industrial refuse is 5:2:3。
7. according to claim 4 a kind of by domestic waste and industry organic waste mixing manufacture biomass fuel technique, be characterised by, described step 5. in, the mass ratio of A class rubbish, B class rubbish and industrial refuse is 4:1:5。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410694992.2A CN105689356B (en) | 2014-11-27 | 2014-11-27 | A kind of technique that domestic waste and industrial organic waste are mixed into manufacture biomass fuel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410694992.2A CN105689356B (en) | 2014-11-27 | 2014-11-27 | A kind of technique that domestic waste and industrial organic waste are mixed into manufacture biomass fuel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105689356A true CN105689356A (en) | 2016-06-22 |
| CN105689356B CN105689356B (en) | 2018-05-22 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410694992.2A Expired - Fee Related CN105689356B (en) | 2014-11-27 | 2014-11-27 | A kind of technique that domestic waste and industrial organic waste are mixed into manufacture biomass fuel |
Country Status (1)
| Country | Link |
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| CN (1) | CN105689356B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111253991A (en) * | 2020-03-27 | 2020-06-09 | 刘国庆 | Biomass fuel processing method and processing system |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1434002A (en) * | 2003-03-05 | 2003-08-06 | 湖南大学 | Deodorant, modified deodorant and deodorizing method for refuse compost |
| EP1837089A2 (en) * | 2006-03-21 | 2007-09-26 | IMA Sanierungszentren GbR bestehend aus den Gesellschaftern BPG Ges. für Bauplanung u. Umwelttechnik mbH, Frankfurt a. M. und Wayss & | Method for rendering the fine mixed sieve fractions from industrial, commercial and residential waste disposable |
| CN101947535A (en) * | 2010-08-03 | 2011-01-19 | 刘刚 | Harmless ecological environmental-protection recycling method of organic food wastes |
| CN102690133A (en) * | 2012-06-14 | 2012-09-26 | 南京信息职业技术学院 | Method for producing organic fertilizer by utilizing garbage |
| CN102936524A (en) * | 2011-08-15 | 2013-02-20 | 朱学智 | Garbage sorting disposal system and garbage disposal method for the same |
| CN103264042A (en) * | 2013-05-29 | 2013-08-28 | 冯国恒 | Household garbage recycling method |
| KR20130124429A (en) * | 2012-05-04 | 2013-11-13 | (주)포레코 | Solid fuel making equipment using livestock excretions |
-
2014
- 2014-11-27 CN CN201410694992.2A patent/CN105689356B/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1434002A (en) * | 2003-03-05 | 2003-08-06 | 湖南大学 | Deodorant, modified deodorant and deodorizing method for refuse compost |
| EP1837089A2 (en) * | 2006-03-21 | 2007-09-26 | IMA Sanierungszentren GbR bestehend aus den Gesellschaftern BPG Ges. für Bauplanung u. Umwelttechnik mbH, Frankfurt a. M. und Wayss & | Method for rendering the fine mixed sieve fractions from industrial, commercial and residential waste disposable |
| CN101947535A (en) * | 2010-08-03 | 2011-01-19 | 刘刚 | Harmless ecological environmental-protection recycling method of organic food wastes |
| CN102936524A (en) * | 2011-08-15 | 2013-02-20 | 朱学智 | Garbage sorting disposal system and garbage disposal method for the same |
| KR20130124429A (en) * | 2012-05-04 | 2013-11-13 | (주)포레코 | Solid fuel making equipment using livestock excretions |
| CN102690133A (en) * | 2012-06-14 | 2012-09-26 | 南京信息职业技术学院 | Method for producing organic fertilizer by utilizing garbage |
| CN103264042A (en) * | 2013-05-29 | 2013-08-28 | 冯国恒 | Household garbage recycling method |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111253991A (en) * | 2020-03-27 | 2020-06-09 | 刘国庆 | Biomass fuel processing method and processing system |
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| CN105689356B (en) | 2018-05-22 |
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