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WO2013172661A1 - Procédé de production de combustible solide écologique et très efficace au moyen de déchets organiques à forte teneur en eau, et système de puissance et de chaleur combiné utilisant ledit procédé - Google Patents

Procédé de production de combustible solide écologique et très efficace au moyen de déchets organiques à forte teneur en eau, et système de puissance et de chaleur combiné utilisant ledit procédé Download PDF

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Publication number
WO2013172661A1
WO2013172661A1 PCT/KR2013/004323 KR2013004323W WO2013172661A1 WO 2013172661 A1 WO2013172661 A1 WO 2013172661A1 KR 2013004323 W KR2013004323 W KR 2013004323W WO 2013172661 A1 WO2013172661 A1 WO 2013172661A1
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reactor
waste
solid fuel
organic waste
functional organic
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Ceased
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PCT/KR2013/004323
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English (en)
Korean (ko)
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하재현
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Priority to RU2014145949/04A priority Critical patent/RU2586332C1/ru
Priority to ES201490128A priority patent/ES2526716B1/es
Priority to CN201380025548.5A priority patent/CN104508093A/zh
Priority to US14/401,607 priority patent/US20150143809A1/en
Publication of WO2013172661A1 publication Critical patent/WO2013172661A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/40—Solid fuels essentially based on materials of non-mineral origin
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/40—Solid fuels essentially based on materials of non-mineral origin
    • C10L5/403—Solid fuels essentially based on materials of non-mineral origin on paper and paper waste
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L5/00—Solid fuels
    • C10L5/40—Solid fuels essentially based on materials of non-mineral origin
    • C10L5/406—Solid fuels essentially based on materials of non-mineral origin on plastic
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • 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
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L9/00—Treating solid fuels to improve their combustion
    • C10L9/08—Treating solid fuels to improve their combustion by heat treatments, e.g. calcining
    • C10L9/086—Hydrothermal carbonization
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
    • F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
    • F01K25/14—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours using industrial or other waste gases
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L2200/00—Components of fuel compositions
    • C10L2200/04—Organic compounds
    • C10L2200/0461—Fractions defined by their origin
    • C10L2200/0469—Renewables or materials of biological origin
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L2270/00—Specifically adapted fuels
    • C10L2270/04—Specifically adapted fuels for turbines, planes, power generation
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/08—Drying or removing water
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/24—Mixing, stirring of fuel components
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/28—Cutting, disintegrating, shredding or grinding
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/48—Expanders, e.g. throttles or flash tanks
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/50—Screws or pistons for moving along solids
    • 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 method for producing a solid raw material from high-functional organic wastes while significantly reducing odor, and a cogeneration system using the same.
  • Organic wastes such as organic sludge and livestock manure are treated using technologies such as incineration, fermentation and direct and indirect drying.
  • incineration generates disadvantageous substances such as dioxins, requires a large amount of external energy, and is expensive due to high installation costs.
  • the direct and indirect drying has a problem that a considerable amount of energy is consumed to lower the moisture of 80% to 15%, and the bad smell is generated in the solid fuel after drying and drying.
  • the occurrence of such odor is particularly severe, there is a problem that the energy efficiency is low, takes a lot of time and wastewater treatment.
  • marine discharges are banned from sewage sludge and livestock manure since January 2012. Also, from January 2013, marine dumping will be banned for wastewater generated during food waste disposal.
  • the present invention is to provide a cogeneration system using the solid fuel prepared above as a problem.
  • the present invention for solving the above problems as one aspect,
  • the present invention relates to a cogeneration system using the solid fuel produced by the above method.
  • the present invention by mixing high-functional organic waste and municipal waste into the Fe-based reactor and mixing and adding high-temperature, high-pressure steam, organic matter and odor components due to decomposition of steam radicals and peptone reactions by Fe reaction catalysts are highly By effectively decomposing and rapidly decomposing organic wastes, the organic wastes are crushed and completely decomposed to efficiently dry the internal wastes of the organic wastes to prepare solid fuels.
  • the high-pressure and high-pressure steam is applied to reduce the molecular weight of the undecomposed organic waste, and to expand the municipal waste to increase the specific surface area, thereby greatly improving drying efficiency. There is an effect that can be produced in a solid fuel in time.
  • the solid fuel produced by the method of the present invention can be provided as an excellent energy source to replace the fossil energy because the low calorific value, there is an effect that can be efficiently produced by the cogeneration system using the same.
  • FIG. 1 shows a treatment system for a high functional organic waste according to the present invention.
  • Figure 2 shows the ionic change and the dielectric constant change curve of the water.
  • the present invention relates to a method for manufacturing solid fuel using high-efficiency organic waste of eco-friendly and high efficiency, which crushes and completely decomposes organic wastes by a rapid depressurization process so as to efficiently dry them to the internal water of organic wastes.
  • the present invention is a (a) mixing step of mixing the high-functional organic waste and municipal waste into the Fe-based reactor for mixing; (b) hydrolysis of hydrolyzing the mixture by adding hot steam to the reactor to pressurize the mixture of the organic waste and municipal waste, and then stirring the mixture in a pressurized state; (c) reducing the molecular weight of the organic wastes from step (b) by squeezing the reactor inside by rapidly depressurizing and leaving the steam inside the reactor, or by increasing the specific surface area of the municipal wastes from step (b) Decompression step; (d) applying a vacuum or differential pressure condition to the reactor to remove moisture from the reactants passed through step (c); And (e) a solid fuelization step of naturally drying the reactants passed through the step (d) to produce a solid fuel having a water content of 10 to 20%; and comprising a solid fuel manufacturing method using a high functional organic waste.
  • the step (a) is a step of mixing the high-functional organic waste and the waste mixed with municipal waste in the Fe-based reactor, the high-functional organic waste is selected from livestock manure, sewage sludge, food waste At least one of them is a waste having a water content of 80% or more, and the municipal waste preferably includes papers and plastics.
  • the paper is 50 to 55% by weight of the municipal waste, plastics to include 40 to 45% by weight.
  • the high-functional organic waste and municipal waste are more preferably mixed at a ratio of 3.5-4: 0.5-1.
  • the high-functional organic waste and municipal waste are mixed into the reactor at a filling rate of 70 to 90%. It is possible to maintain the efficiency of the reaction by maximizing the processing capacity of the waste because high temperature and high pressure water vapor can be supplied from the outside of the reactor to maintain contact reaction with saturated steam even if the desired waste is introduced into the reactor at the high filling rate as described above. You can increase it.
  • the step (b) is a step of hydrolyzing the mixture by stirring in a pressurized state after pressurizing the mixture of the organic waste and municipal waste by applying a high temperature steam to the reactor, by pressing It is a step of lowering the moisture content of the organic waste by high temperature while decomposing the constituents of the organic waste to low molecular weight, decomposing odor components including sulfuric acid component to remove the odor.
  • a boiler connected to the reactor by applying a steam of 200 ⁇ 250 °C to the reactor to the internal pressure of the reactor to 20 to 25 atm, and then by agitating the hydrolysis reaction is made. As shown in FIG.
  • the present invention is to supply the steam in the step (b) by using a boiler connected to the reactor, without the process of changing to hot water by direct contact injection to the organic waste of low temperature,
  • the organic wastes can come into contact with the water vapor supplied from the boiler and cause a physicochemical reaction, thereby significantly improving the efficiency of the reaction.
  • the phenomenon of reacting with hot water does not occur by supplying steam using a boiler supplied from the outside as described above, the reaction can be maintained even if the amount of waste charged in the reactor is increased, and the mixture of waste to be treated It can be charged to reach 70-90% of the reactor to cause a contact reaction with water vapor.
  • the catalytic action of Fe can promote the peptone reaction, particularly in the region occupied by saturated steam in the reactor, thereby significantly increasing the efficiency of the reaction.
  • an organic film of 1 to 2 mm is formed inside the reactor so that corrosion by NaCl or the like can be prevented.
  • the step (c) is to discharge the vapor inside the reactor to rapidly reduce the inside of the reactor to stand to lower the molecular weight of the organic waste, which has passed the step (b), or (b)
  • the specific surface area of municipal waste is increased to crush.
  • This step is to reduce the molecular weight or crush by increasing the volume by temporarily depressurizing the reactant under high pressure.
  • the volume of urban garbage as a raw material expands instantaneously, and the specific surface area is increased, so that the drying time is considerably shortened as it reacts with the water-containing organic material, thereby significantly improving the drying efficiency.
  • the step (d) is to remove the water of the reactants passed through the step (c) by applying a vacuum or differential pressure condition to the reactor, preferably by using a vacuum pump connected to the reactor.
  • a vacuum or a differential pressure condition for 10 to 15 minutes to the reactor is characterized in that to remove 5 to 10% of the moisture contained in the reactant passed through the step (c).
  • the step (e) is a step of producing a solid fuel having a water content of 10 to 20% by naturally drying the reactants passed through the step (d), preferably low calorific value of 5000 kcal / kg or more It is characterized by producing a solid fuel having.
  • the present invention relates to a cogeneration system using the solid fuel produced by the above method. That is, the present invention produces a solid fuel (RDF) from the high-functional organic waste and municipal waste and supplies it to the RDF burner and boiler to produce superheated steam and to produce electric power by the steam power generation system using the superheated steam. It will be able to provide a cogeneration system that can do this.
  • RDF solid fuel
  • the reaction mixture was stirred at 10 to 15 rpm to produce a physicochemical reaction between the water vapor and the waste.
  • saturated steam or superheated steam was intermittently supplied to maintain the atmosphere at 210 ° C. and 23 atm.
  • the above state is organically treated for about 30 to 60 minutes depending on the properties of the object to be treated to sufficiently generate a peptone reaction by the catalytic action of water vapor, the organic material to be treated, and the Fe-based reactor.
  • the pressure relief valve was opened and vapor was instantaneously discharged through the steam outlet until it reached atmospheric pressure (1 atm) within 2 minutes so that organic matter, organic cells, or MSW that were not decomposed during the above reaction were low-molecularized or crushed.
  • a vacuum (differential pressure) process is performed for about 10 to 15 minutes using an external vacuum (differential pressure) pump to remove water in the reactor under high temperature vacuum or differential pressure conditions. About 5-10% were removed.
  • the product produced after the reaction was transferred to a paddle-type dry plant and then dried naturally to produce a final solid fuel having a water content of 15%.
  • Solid fuel was prepared by the method of Example 1, but solid fuel was prepared without adding municipal waste (MSW).
  • Solid fuel was prepared by the method of Example 1, but solid fuel was prepared without undergoing a process of suddenly depressurizing the steam after pressurizing.
  • Example 1 (wt%) Comparative Example 1 (wt%) Comparative Example 2 (wt%) 0 83 59 84 60 10 80 36 81 47 20 77 10 75 36 40 65 5 63 22 60 61 4 56 15
  • Example 1 the results of analyzing the characteristics of the municipal waste used in Example 1 and Comparative Example 2 are as follows.
  • the average of 5,000 kcal / kg of the case of Example 1 with the addition of municipal waste is about 500 kcal / kg
  • the calorific value was shown. That is, more than 50% of papers and 40% or more of plastics contained in urban waste improves the specific surface area in a sudden reduction process, thereby increasing the drying speed, and also generating calorific value of solid products by the petroleum-based organic plastics. It seems to be able to increase.
  • the average calorific value is shown in Table 3 below. (Unit: kcal / kg)

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Processing Of Solid Wastes (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
PCT/KR2013/004323 2012-05-17 2013-05-15 Procédé de production de combustible solide écologique et très efficace au moyen de déchets organiques à forte teneur en eau, et système de puissance et de chaleur combiné utilisant ledit procédé Ceased WO2013172661A1 (fr)

Priority Applications (4)

Application Number Priority Date Filing Date Title
RU2014145949/04A RU2586332C1 (ru) 2012-05-17 2013-05-15 Экологически чистый и высокоэффективный способ получения твердого топлива с использованием органических отходов с высоким содержанием воды и комбинированная теплоэлектрическая система с использованием данного способа
ES201490128A ES2526716B1 (es) 2012-05-17 2013-05-15 Procedimiento de producción de combustibles sólidos de alta eficacia y respetuoso con el medio ambiente que usa residuos orgánicos de alto contenido en agua, y sistema combinado de energía térmica y energía eléctrica que usa dicho procedimiento.
CN201380025548.5A CN104508093A (zh) 2012-05-17 2013-05-15 环保高效的利用高含水有机废弃物制备固体燃料的方法以及利用该方法的热电联产系统
US14/401,607 US20150143809A1 (en) 2012-05-17 2013-05-15 Environmentally friendly and high efficiency solid fuel production method using high-water-content organic waste, and combined heat and power system using same

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR10-2012-0052662 2012-05-17
KR1020120052662A KR101313314B1 (ko) 2012-05-17 2012-05-17 고함수 유기성 폐기물을 이용한 친환경·고효율의 고형연료 제조방법 및 이를 이용한 열병합 발전 시스템

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WO2013172661A1 true WO2013172661A1 (fr) 2013-11-21

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US (1) US20150143809A1 (fr)
KR (1) KR101313314B1 (fr)
CN (1) CN104508093A (fr)
ES (1) ES2526716B1 (fr)
RU (1) RU2586332C1 (fr)
WO (1) WO2013172661A1 (fr)

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CN106753676A (zh) * 2017-01-03 2017-05-31 苏州草宝能源科技有限公司 一种高温湿法干燥生活垃圾的方法
CN109943380A (zh) * 2019-02-22 2019-06-28 佐古猛 一种固体燃料制造方法及制造装置
KR102107704B1 (ko) * 2019-05-22 2020-05-07 주식회사 네오디아 하수 슬러지를 이용한 연료 제조장치
JP7285729B2 (ja) * 2019-08-08 2023-06-02 三菱重工業株式会社 廃棄物処理装置
CN110564431B (zh) * 2019-09-10 2024-07-12 上海环境卫生工程设计院有限公司 一种湿垃圾脱水热解方法及系统
CN111112276A (zh) * 2019-11-25 2020-05-08 林赞德 废弃物处理方法
KR102198208B1 (ko) 2020-07-13 2021-01-04 채재우 고함수 웨이스트 재활용 및 소각장치
KR102319903B1 (ko) * 2020-12-03 2021-11-01 하재현 생활 쓰레기 가수 분해 펠렛 연료화 시스템
CN114433596B (zh) * 2022-01-25 2023-04-18 上海汉怡环保科技有限公司 一种有机质垃圾处理工艺
CN116179251B (zh) * 2023-04-19 2025-05-13 尚微生态科技有限公司 一种基于工业废料制备燃料的方法
KR102814867B1 (ko) 2023-12-12 2025-05-30 이만숙 바이오 고형원료 생산용 함수율 조절 기능이 있는 스팀 열 가수분해 반응기

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KR101313314B1 (ko) 2013-09-30
ES2526716A2 (es) 2015-01-14
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ES2526716R1 (es) 2015-02-04
CN104508093A (zh) 2015-04-08
ES2526716B1 (es) 2015-11-17

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