WO2022092358A1 - 유기성 폐기물 발효 부산물을 이용한 고형연료 제조 시스템 - Google Patents
유기성 폐기물 발효 부산물을 이용한 고형연료 제조 시스템 Download PDFInfo
- Publication number
- WO2022092358A1 WO2022092358A1 PCT/KR2020/014962 KR2020014962W WO2022092358A1 WO 2022092358 A1 WO2022092358 A1 WO 2022092358A1 KR 2020014962 W KR2020014962 W KR 2020014962W WO 2022092358 A1 WO2022092358 A1 WO 2022092358A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fermentation
- drying
- products
- solid fuel
- hot air
- Prior art date
Links
- 238000000855 fermentation Methods 0.000 title claims abstract description 86
- 230000004151 fermentation Effects 0.000 title claims abstract description 86
- 239000006227 byproduct Substances 0.000 title claims abstract description 28
- 239000004449 solid propellant Substances 0.000 title claims abstract description 22
- 239000010815 organic waste Substances 0.000 title claims abstract description 21
- 238000002360 preparation method Methods 0.000 title abstract 3
- 238000001035 drying Methods 0.000 claims abstract description 52
- 239000008188 pellet Substances 0.000 claims description 42
- 239000002699 waste material Substances 0.000 claims description 21
- 238000004519 manufacturing process Methods 0.000 claims description 13
- 239000002028 Biomass Substances 0.000 claims description 9
- 239000000446 fuel Substances 0.000 claims description 9
- 239000003638 chemical reducing agent Substances 0.000 claims description 8
- 230000000813 microbial effect Effects 0.000 claims description 8
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 239000010871 livestock manure Substances 0.000 abstract description 5
- 239000010794 food waste Substances 0.000 abstract description 3
- 239000010801 sewage sludge Substances 0.000 abstract description 2
- 235000019645 odor Nutrition 0.000 description 15
- 238000000034 method Methods 0.000 description 9
- 238000000465 moulding Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 238000001599 direct drying Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- 238000010564 aerobic fermentation Methods 0.000 description 1
- 238000004887 air purification Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/34—Other details of the shaped fuels, e.g. briquettes
- C10L5/36—Shape
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/42—Solid fuels essentially based on materials of non-mineral origin on animal substances or products obtained therefrom, e.g. manure
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/46—Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H3/00—Air heaters
-
- 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
Definitions
- the present invention relates to a solid fuel manufacturing system using by-products after fermentation reduction treatment of wet organic waste (food waste, livestock manure, sewage sludge, etc.) It is a technology related to a solid fuel manufacturing system using organic waste fermentation-drying and by-products with a function of removing the generated trace odor.
- an indirect drying method which can reduce fuel costs as opposed to the direct drying method, but has a problem in that it takes a lot of time and generates a large amount of odor.
- the natural fermentation drying method uses self-heating to dry it, but there is a problem in that a large amount of odor is generated for a long period of time due to the decay of some wastes during long-term fermentation. These odors require an air purification process, and thus are accompanied by expensive reprocessing and civil complaints.
- the method related to the present invention is an indirect drying method using a specially designed and manufactured fermentor and fermentation by a specified microorganism, and can be dried faster than the existing fermentation method, low-cost continuous operation is possible under odor-free conditions, and the efficiency can be increased suggests a way to do it.
- the present invention reduces the dry fuel cost by applying the microbial fermentation drying method, and uses the by-product obtained through the organic waste fermentation apparatus to reduce the odor generated during the drying process in an environmentally friendly way (using)
- An object of the present invention is to provide a biomass solid fuel manufacturing system that can be recycled and recycled.
- the present invention provides a storage tank in which waste is accommodated; Fermentation drying loss machine for receiving the waste from the storage tank and drying it by microbial fermentation by the pre-injected fermenting agent to produce fermentation by-products; a pellet forming machine for receiving the fermentation by-products from the fermentation drying loss machine and forming them into pellets; A portion of the solid fuel produced in the pellet forming machine is transferred, used as incineration fuel, and fresh hot air exchanged with heat generated by incineration is supplied to the fermentation drying reducer, and the gas generated by fermentation and drying in the fermentation drying reducing unit. It provides a solid fuel manufacturing system using organic waste fermentation by-products, characterized in that it includes; a pellet hot air boiler that receives inflow and removes residual odors by incineration heat.
- the fermentation drying loss machine is provided with a stirrer therein, so that the waste and the fermentation accelerator can be stirred by itself inside the fermenter.
- the pellet hot air boiler using fuel as pellets produced in the pellet forming machine at an outlet temperature of 850 ° C. or higher, incinerates the odor discharged from the fermentation drying reducer at a high temperature, and in the fermentation drying reducer about 50 ° C. to It is characterized in that the hot air is provided at a temperature of 80°C.
- pellet hot air boiler air is introduced from the outside and the pellet hot air boiler generates the hot air by incineration heat of the pellet hot air boiler, characterized in that it is supplied to the fermentation drying reduction unit.
- a moisture dryer and a biomass mixer are further provided.
- wet organic waste which is generally difficult to treat, can be produced as an eco-friendly biomass solid fuel through dry compression after fermentation loss.
- the slight residual odor generated during the fermentation process can be burned in the biomass pellet hot air boiler produced in this process to completely eliminate the odor.
- FIG. 1 is a flowchart of a solid fuel manufacturing system using organic waste fermentation by-products according to an embodiment of the present invention.
- FIG. 1 is a flowchart of a solid fuel manufacturing system using organic waste fermentation by-products according to an embodiment of the present invention.
- the solid fuel manufacturing system using the organic waste fermentation by-product of the present invention is largely composed of a storage tank 100, a fermentation drying loss machine 200, a pellet molding machine 300 and a pellet hot air boiler 400. Waste Through this sequential process, solid fuel can be produced. And, if necessary, a moisture dryer 210 and a biomass mixer 220 may be further added between the fermentation drying reduction machine 200 and the pellet forming machine 300 . In the present invention, there are major characteristics in the fermentation drying reduction unit 200 and the pellet hot air boiler 400 .
- the storage tank 100 is a tank in which waste is accommodated and stored.
- the waste corresponds to food waste, dewatered sludge from sewage treatment plant, livestock manure, livestock manure by-product, etc., and is a high-moisture wet organic waste that can react with microorganisms.
- the fermentation drying loss machine 200 is a device capable of fermenting and drying the waste.
- the fermentation drying reduction unit 200 receives the waste from the storage tank 100 and is dried by high-speed fermentation by the pre-injected microbial medium to produce fermentation by-products.
- the fermenting agent will include wood flour and a microbial growth fermentation accelerator.
- the fermentation drying loss machine 200 is provided with a stirrer therein, it is characterized in that the waste and the fermentation accelerator can be stirred by itself.
- a pair of the agitators are installed facing each other in a screw shaft type, and by rotation, the waste located at the upper part moves to the lower side and the lower waste moves to the upper side, so that the fermentation promoter is evenly stirred, and air is introduced so that oxygen contact is made smoothly
- a device can be built-in to improve fermentation efficiency.
- the pellet molding machine 300 is a device for molding the fermentation by-product into pellets by extrusion.
- biomass such as wood chips and sometimes waste plastic powder are added in the middle, mixed in a high-speed biomass dryer 220, and dried to pellet (pellet) ) can supplement the calorific value. This is to match the thermal efficiency of the pellets to be molded.
- the pellet hot air boiler 400 burns the pellets at an outlet temperature of 850° C. or higher to incinerate and remove the odor generated in the fermentation drying reduction unit 200 .
- the odor generated inside the fermentation process can be incinerated and treated, as well as each device must be connected.
- pellet hot air boiler 400 can increase the fermentation efficiency by supplying fresh hot air to the fermentation drying reduction unit 200 .
- the solid fuel produced in the pellet molding machine 300 is transferred and used as incineration fuel.
- the heat generated by incineration causes the fresh hot air generated by the heat exchange to be supplied to the fermentation drying loss reducer 200 inside.
- the hot air is air introduced from the outside of the pellet hot air boiler 400, and as the air passes through the pellet hot air boiler 400, heat is exchanged with the heat of the pellet hot air boiler 400 to generate hot air and to the fermentation drying loss reducer 200. can be supplied.
- the hot air is supplied to the fermentation-drying reducer 200 at a temperature of about 50° C. to 80° C., so that the waste is provided under optimal conditions for fermentation, thereby promoting high-speed fermentation. If it exceeds 80 °C, the microorganisms disappear, and if it is less than 50 °C, the microbial activity is slowed.
- pellet hot air boiler 400 the steam generated by fermentation and drying in the fermentation and drying reduction unit 200 is condensed and the separated residual odor gas is connected to the combustion air passage to incinerate the odor inside the pellet hot air boiler. can be removed
- an atmospheric prevention facility 500 is additionally connected to the pellet hot air boiler 400 to filter contaminants by a filter and to remove residual odors once more.
- the fermentation agent is pre-injected into the fermentation-drying reduction unit 200, and after inputting wastes having a moisture content of about 80%, the fermentation by-products are stirred and fermented for about 24 hours to produce a fermentation by-product with a moisture content of 55% or less.
- the reason for maintaining the moisture content at 55% is that these fermentation by-products can be used as compost raw materials to be composted through secondary fermentation and fermentation after mixing with livestock manure by maintaining microbial activity.
- the fermentation by-products treated for reduced fermentation are discharged and dried to less than 20% moisture content, dried and compressed to produce a biomass solid raw material, and the rest is stored in the fermentation-drying loss machine 200 to reduce the moisture content to 55% or less.
- high microbial activity it acts as a fermentation promoter, and by inputting waste, the waste is repeatedly fermented and dried, and fermentation by-products are continuously produced.
- the present invention is based on a basic technical basis for a solid fuel manufacturing system using organic waste fermentation by-products.
- a basic technical basis for a solid fuel manufacturing system using organic waste fermentation by-products is based on a basic technical basis for a solid fuel manufacturing system using organic waste fermentation by-products.
- many other variations are possible for the ruler.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Description
Claims (5)
- 폐기물이 수용되는 저장탱크(100);상기 저장탱크의 폐기물을 이송받고 선 투입된 발효제에 의해 미생물 발효로 건조하여 발효부산물을 생성하는 발효건조 감량기(200);상기 발효건조 감량기에서 상기 발효부산물을 이송받아 펠릿(pellet)으로 성형하는 펠릿 성형기(300);상기 펠릿 성형기에서 생산된 고체연료 일부를 이송받아 소각연료로 사용되고 소각에 의해 발생된 열과 열교환된 신선한 열풍을 상기 발효건조 감량기로 공급되게 하고, 상기 발효건조 감량기에서 발효 및 건조에 의해 발생된 기체를 유입받아 소각열에 의해 잔류 악취를 제거하는 펠릿 열풍보일러(400);가 포함되는 것을 특징으로 하는 유기성 폐기물 발효 부산물을 이용한 고형연료 제조 시스템.
- 제1항에 있어서,상기 발효건조 감량기(200)는,내부에 교반기가 구비되어 상기 폐기물과 발효촉진제가 발효조 내부에서 자체적으로 교반 가능한 것을 특징으로 하는 유기성 폐기물 발효 부산물을 이용한 고체연료 제조 시스템.
- 제1항에 있어서,상기 펠릿 열풍보일러(400)는,상기 펠릿 성형기에서 생산된 펠릿으로 연료를 사용하여 출구온도 850℃ 이상의 고온으로 상기 발효건조 감량기에서 배출되는 악취를 고온으로 소각 소멸되게 하고,상기 발효건조 감량기에 약 50℃ 내지 80℃ 온도로 상기 열풍을 제공하는 것을 특징으로 하는 유기성 폐기물 발효 부산물을 이용한 고형연료 제조 시스템.
- 제1항에 있어서,상기 펠릿 열풍보일러(400)에는,외부에서 공기가 유입되고 상기 펠릿 열풍보일러의 소각열에 의해 상기 펠릿 열풍보일러에서 상기 열풍을 생성하여 상기 발효건조 감량기에 공급되는 것을 특징으로 하는 유기성 폐기물 발효 부산물을 이용한 고형연료 제조 시스템.
- 제1항에 있어서,상기 발효건조 감량기(200)와 펠릿 성형기(300) 사이에는,수분건조기(210)와 바이오매스 혼합기(220)가 더 구비되는 것을 특징으로 하는 유기성 폐기물 발효 부산물을 이용한 고형연료 제조 시스템.
Applications Claiming Priority (2)
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KR20200141307 | 2020-10-28 | ||
KR10-2020-0141307 | 2020-10-28 |
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Publication Number | Publication Date |
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WO2022092358A1 true WO2022092358A1 (ko) | 2022-05-05 |
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PCT/KR2020/014962 WO2022092358A1 (ko) | 2020-10-28 | 2020-10-29 | 유기성 폐기물 발효 부산물을 이용한 고형연료 제조 시스템 |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114989874A (zh) * | 2022-07-04 | 2022-09-02 | 宁夏瑞创源新能源科技有限公司 | 一种葡萄枝沼渣生物质颗粒燃料制备工艺 |
KR102568376B1 (ko) * | 2022-09-14 | 2023-08-23 | 바이오씨앤씨(주) | 축분 에너지 펠렛 및 축분 바이오차의 제조방법 |
Citations (5)
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JP2001347249A (ja) * | 2000-06-08 | 2001-12-18 | Kiyomoto Bio Co Ltd | 有機廃棄物高速処理方法 |
JP2013017926A (ja) * | 2011-07-08 | 2013-01-31 | Syudensya Co Ltd | 有機性廃棄物処理装置 |
KR20130124429A (ko) * | 2012-05-04 | 2013-11-13 | (주)포레코 | 축산분뇨를 이용한 고형연료화장치 |
KR20160079731A (ko) * | 2016-05-13 | 2016-07-06 | 주식회사 일엽지추 | 낙엽 펠릿의 제조 공정 및 성형기 |
KR102052924B1 (ko) * | 2019-01-31 | 2019-12-11 | 주식회사 우람 | 소각로 일체형 음식물 쓰레기 감량장치 |
-
2020
- 2020-10-29 WO PCT/KR2020/014962 patent/WO2022092358A1/ko active Application Filing
Patent Citations (5)
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JP2001347249A (ja) * | 2000-06-08 | 2001-12-18 | Kiyomoto Bio Co Ltd | 有機廃棄物高速処理方法 |
JP2013017926A (ja) * | 2011-07-08 | 2013-01-31 | Syudensya Co Ltd | 有機性廃棄物処理装置 |
KR20130124429A (ko) * | 2012-05-04 | 2013-11-13 | (주)포레코 | 축산분뇨를 이용한 고형연료화장치 |
KR20160079731A (ko) * | 2016-05-13 | 2016-07-06 | 주식회사 일엽지추 | 낙엽 펠릿의 제조 공정 및 성형기 |
KR102052924B1 (ko) * | 2019-01-31 | 2019-12-11 | 주식회사 우람 | 소각로 일체형 음식물 쓰레기 감량장치 |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN114989874A (zh) * | 2022-07-04 | 2022-09-02 | 宁夏瑞创源新能源科技有限公司 | 一种葡萄枝沼渣生物质颗粒燃料制备工艺 |
KR102568376B1 (ko) * | 2022-09-14 | 2023-08-23 | 바이오씨앤씨(주) | 축분 에너지 펠렛 및 축분 바이오차의 제조방법 |
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