WO2015133682A1 - 가연성 폐기물을 이용한 비성형 고형연료 제조방법 - Google Patents
가연성 폐기물을 이용한 비성형 고형연료 제조방법 Download PDFInfo
- Publication number
- WO2015133682A1 WO2015133682A1 PCT/KR2014/005037 KR2014005037W WO2015133682A1 WO 2015133682 A1 WO2015133682 A1 WO 2015133682A1 KR 2014005037 W KR2014005037 W KR 2014005037W WO 2015133682 A1 WO2015133682 A1 WO 2015133682A1
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- WIPO (PCT)
- Prior art keywords
- waste
- separator
- solid fuel
- particle size
- separated
- Prior art date
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Classifications
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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, 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
-
- 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
- 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/40—Applying a magnetic field or inclusion of magnets in the apparatus
-
- 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
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
- C10L2290/546—Sieving for separating fractions, components or impurities during preparation or upgrading of a fuel
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- 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 non-molded solid fuel using flammable waste, and more particularly, to a crushing crusher for sorting combustible waste in input waste, a primary magnetic separator, a first vibratory multi-stage particle size sorter, an impact crusher, and two.
- High speed thrust crusher, 4th magnetic separator, non-ferrous separator, 2nd vibratory multi-stage granulator In this way, the solid fuel production yield can be maximized as compared to the input waste, and the ferrous metal is selected using a fourth magnetic separator in a mixture of the waste discharged from the high-speed induction mill and the heavy material separated from the wind separator.
- Non-ferrous metals are sorted from the waste discharged from the 4th magnetic separator
- Non-molded using a flammable waste to generate Yun relates to a solid fuel production method.
- the particle size sorting using trommel is carried out the process of introducing small particle sized wastes into particle size using disk screen and vibrating screen, and separating the ferrous metals and non-ferrous metals into the wind selector.
- the method of producing solid fuel by using this method was mainly used or a method of modifying it was mainly used.
- Patent No. 10-1270936 2013.05.29
- Patent No. 10-0921691 2009.10.07
- An object of the present invention has been made in order to solve the above problems, crushing waste for sorting combustible waste in the input waste, primary magnetic separator, primary vibration multi-stage particle size separator, impact crusher, secondary magnetic separator, wind classifier , 3rd magnetic separator, grinder and 1st vibratory multi-stage particle sizer, equipped with high-speed force grinder, 4th magnetic force sorter, non-ferrous separator, 2nd vibratory multi-stage particle size sorter for sorting small particle size
- Non-molded solid fuel manufacturing method using a combustible waste for achieving the above object, (a) the first step of crushing the incoming waste for producing the combustible waste into a non-molded solid fuel using a shredder; (b) separating iron from the primary crushed waste in step (a) using a primary magnetic separator; (c) selecting the particle size of the waste from which iron is separated in step (b) by using a first vibratory multi-stage particle size separator; (d) after the particle size screening in step (c), using the impact crusher to crush the waste having a large particle size; (e) separating iron from the secondary crushed waste using a secondary magnetic separator; (f) sorting the waste from which iron is separated in step (e) by weight using a wind separator; (g) separating iron from the light weight separated in step (f) using a third magnetic separator; And (h) pulverizing the waste from which iron is separated in step (g) with a grinder to produce a solid fuel; It is configured to
- the iron metal separated through the 1,2,3rd magnetic separator is mixed with the waste discharged from the first vibratory multi-stage particle size separator and introduced into the high-speed thrust mill. It is done.
- the waste introduced into the high-speed thrust mill is characterized by separating the iron metal and the tangled waste by using the high-speed thrust mill, and separating the waste having the mixed properties by phase.
- the waste discharged from the high-speed induction crusher is mixed with the heavy material separated in the wind separator, and characterized in that the iron metal is selected using a fourth magnetic separator.
- the waste discharged from the fourth magnetic separator is characterized in that non-ferrous metals are selected using a non-ferrous separator.
- the waste discharged from the non-ferrous separator is classified by particle size by a predetermined size using a second vibratory multi-stage particle size separator, and waste having a particle size of a predetermined size or less is discharged as a residue, and waste having a particle size of a predetermined size or more.
- the primary vibratory multi-stage particle size separator is characterized in that the sieve (Sieve) having a predetermined size is provided.
- the secondary vibratory multi-stage particle size separator is characterized in that the sieve having a smaller size than the checker of the primary vibrating multi-stage particle size separator.
- Particle size may be selected based on size (preferably, 10 mm to 30 mm) to increase the amount of solid fuel produced by effectively recovering waste of a predetermined size or more containing a large amount of combustible material.
- the ferrous metal recovered from the 4th magnetic separator can be separated from the ferrous metal and other wastes by using a high-speed magnetic force separator to increase the recovery rate of flammable waste while making profits of ferrous metal. It is possible to solve the problem of not making profits and lowering the recovery rate of flammable waste because it is recovered and discharged in a tangled state with other wastes.
- FIG. 1 is a flowchart illustrating a method for producing an unmolded solid fuel using combustible waste according to the present invention.
- FIG. 2 is a block diagram of a method for producing non-molded solid fuel using combustible waste according to the present invention.
- non-molded solid fuel manufacturing method using the combustible waste disclosed herein can be implemented in various embodiments, it is not limited to the embodiments described herein.
- the primary shredding step (S110) using the crushing rod shredder (b) the iron separation step (S120) using the primary magnetic separator, (c) particle size sorting step (S130) using the first vibrating multi-stage particle size separator, (d) secondary crushing step (S140) using the impact crusher, and (e) iron separation step (S150) using the second magnetic separator And, (f) sorting by weight using a wind separator (S160), (g) separating iron by using a third magnetic separator (S170), and (h) preparing a solid fuel using a grinder (S180). It is configured to include).
- the inflow waste in the form of a pay-as-you-go bag in order to manufacture the combustible waste into the non-molded solid fuel is shredded using the shredding shredder 110 and large Primary shredding of coarse waste such as metal or wood products is carried out.
- the primary vibratory multi-stage particle size separator 130a is provided with a sieve (not shown) having a predetermined size (preferably, a size of 30 mm to 80 mm), and a predetermined size (preferably, 30 mm). Particle size screening should be performed with wastes larger than or equal to 80 mm and wastes smaller than.
- the waste of more than a predetermined size discharged from the primary vibrating multi-stage particle size selector (130a) is to be shredded to a size of 150 mm or less in order to improve the sorting efficiency of the combustible waste in the impact crusher 140, the tangled waste Separation by properties will increase the sorting efficiency for flammable wastes in subsequent processes.
- step (f) In the screening by weight using the wind separator (S160), the waste separated from the iron in step (e) is sorted by weight (heavy weight and light weight) using the wind separator 150.
- the iron may be separated using the third magnetic separator 120c from the light weight separated in the step (f).
- the waste discharged from the tertiary magnetic separator 120c is mixed with the waste of 10 mm to 30 mm or more in size discharged from the secondary vibratory multi-stage particle size separator 130b, and solid fuel of 50 mm or less using the grinder 180. It will be manufactured as.
- the iron metal separated through the first and second magnetic separators 120a, 120b, and 120c is discharged from the primary vibratory multistage particle size selector 130a. It is mixed with waste having a size of 30 mm to 80 mm or less and flows into the high-speed moment grinder 160.
- the waste introduced into the high-speed thrust mill 160 separates the waste metal and the tangled wastes by using the high-speed thrust mill 160, and separates the waste having the mixed properties by each phase into flammable waste in the subsequent process. To facilitate selection.
- the waste discharged from the high-speed force crusher 160 is mixed with the heavy material separated in the wind separator 150, and then the iron metal is selected using the fourth magnetic separator 120d.
- the ferrous metals selected through the fourth magnetic separator 120d may be sold without additional treatment, thereby generating profit.
- the waste discharged from the fourth magnetic separator 120d is used to select the non-ferrous metal using the non-ferrous separator 170.
- the non-ferrous metals selected through the non-ferrous separator 170 may be sold without additional treatment, thereby generating profit.
- the waste discharged from the non-ferrous separator 170 performs a particle size sorting process according to a predetermined size (preferably, a size of 10 mm to 30 mm) using the secondary vibrating multi-stage particle size separator 130b.
- a predetermined size preferably, a size of 10 mm to 30 mm
- wastes having a particle size smaller than or equal to a predetermined size are discharged as remnants because most of non-combustible substances such as earth and sand components are discharged. It is mixed with the waste discharged from the magnetic separator (120d).
- the secondary vibratory multi-stage particle size separator 130b is provided with a sieve having a predetermined size (preferably, a size of 10 mm to 30 mm) to perform particle size selection.
- step (h) in the step of manufacturing the solid fuel using the grinding machine (S180), by grinding the waste iron separated from the iron in step (g) to the mill 180 or less in size It will be made of solid fuel that can produce electricity and steam.
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Combined Means For Separation Of Solids (AREA)
Abstract
Description
Claims (8)
- (a)가연성 폐기물을 비성형 고형연료로 제조하기 위한 유입 폐기물을 파봉파쇄기를 이용하여 1차 파쇄하는 단계;(b)상기 (a)단계에서 1차 파쇄된 폐기물로부터 1차 자력선별기를 이용하여 철류를 분리하는 단계;(c)상기 (b)단계에서 철류가 분리된 폐기물을 1차 진동식 다단 입도선별기를 이용하여 입도 선별하는 단계;(d)상기 (c)단계에서 입도 선별 후, 충격파쇄기를 이용하여 입자가 큰 폐기물을 2차 파쇄하는 단계;(e)2차 파쇄된 폐기물로부터 2차 자력선별기를 이용하여 철류를 분리하는 단계;(f)상기 (e)단계에서 철류가 분리된 폐기물을 풍력선별기를 이용하여 중량별로 선별하는 단계;(g)상기 (f)단계에서 분리된 경량물로부터 3차 자력선별기를 이용하여 철류를 분리하는 단계; 및(h)상기 (g)단계에서 철류가 분리된 폐기물을 분쇄기로 분쇄하여 고형연료를 제조하는 단계;를 포함하는 가연성 폐기물을 이용한 비성형 고형연료 제조방법.
- 제1항에 있어서,상기 (b), (e), (g)단계에서 1,2,3차 자력선별기를 통해 분리된 철류 금속은 1차 진동식 다단 입도선별기에서 배출된 폐기물과 혼합되어 고속타력분쇄기 측으로 유입되는 것을 특징으로 하는 가연성 폐기물을 이용한 비성형 고형연료 제조방법.
- 제2항에 있어서,상기 고속타력분쇄기 측으로 유입된 폐기물은 고속타력분쇄기를 이용하여 철류 금속과 엉킨 폐기물을 분리하고, 성상이 혼합되어 있는 폐기물을 성상별로 분리하는 것을 특징으로 하는 가연성 폐기물을 이용한 비성형 고형연료 제조방법.
- 제1항 또는 제3항에 있어서,상기 고속타력분쇄기에서 배출된 폐기물은 풍력선별기에서 분리된 중량물과 혼합되고, 4차 자력선별기를 이용하여 철류 금속을 선별하는 것을 특징으로하는 가연성 폐기물을 이용한 비성형 고형연료 제조방법.
- 제4항에 있어서,상기 4차 자력선별기에서 배출된 폐기물은 비철선별기를 이용하여 비철류 금속을 선별하는 것을 특징으로 하는 가연성 폐기물을 이용한 비성형 고형연료 제조방법.
- 제5항에 있어서,상기 비철선별기에서 배출된 폐기물은 2차 진동식 다단 입도선별기를 이용하여 기설정된 크기별로 입도 선별하되,기설정된 크기 이하의 입자 크기를 갖는 폐기물은 잔재물로 배출하고, 기설정된 크기 이상의 입자 크기를 갖는 폐기물은 4차 자력선별기에서 배출된 폐기물과 혼합하고 분쇄기를 통해 분쇄하여 고형연료로 제조하는 것을 특징으로 하는 가연성 폐기물을 이용한 비성형 고형연료 제조방법.
- 제1항에 있어서,상기 1차 진동식 다단 입도선별기에는 일정 크기를 갖는 체(Sieve)가 구비되는 것을 특징으로 하는 가연성 폐기물을 이용한 비성형 고형연료 제조방법.
- 제3항 내지 제7항 중 어느 한 항에 있어서,상기 2차 진동식 다단 입도선별기에는 1차 진동식 다단 입도선별기의 체크기보다 작은 크기의 체가 구비되는 것을 특징으로 하는 가연성 폐기물을 이용한 비성형 고형연료 제조방법.
Priority Applications (1)
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US15/124,062 US10047312B2 (en) | 2014-03-07 | 2014-06-09 | Method for manufacturing fluff solid fuel using combustible waste |
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KR10-2014-0027063 | 2014-03-07 | ||
KR1020140027063A KR101574691B1 (ko) | 2014-03-07 | 2014-03-07 | 가연성 폐기물을 이용한 비성형 고형연료 제조방법 |
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US (1) | US10047312B2 (ko) |
KR (1) | KR101574691B1 (ko) |
WO (1) | WO2015133682A1 (ko) |
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CN109097146A (zh) * | 2018-08-07 | 2018-12-28 | 刘树云 | 生活垃圾生物煤质化方法 |
KR102195560B1 (ko) * | 2020-04-29 | 2020-12-28 | 새마을환경개발주식회사 | 건설폐기물의 처리과정에서 소성로를 이용한 연료화 방법 |
KR102148276B1 (ko) * | 2020-06-22 | 2020-08-27 | 주식회사 신텍 | 다중 파봉 및 선별 과정을 포함하는 생활계 폐기물 전처리 방법과 그 장치 |
KR102453847B1 (ko) * | 2020-08-19 | 2022-11-04 | 주식회사 이도 | 건설혼합폐기물 중 가연성 폐기물의 회수율을 높인 고체연료 재활용 자원화 시스템 |
KR102270489B1 (ko) * | 2020-08-31 | 2021-06-29 | 한정근 | 건설폐기물을 파쇄하여 순환골재로 재활용하거나, 쇄석골재를 제조하는 과정에서 이물질 제거 및 골재 세척장치 |
KR102272652B1 (ko) * | 2020-08-31 | 2021-07-05 | 한정근 | 골재를 문질러 이물질을 제거하는 그라블 스크리브 |
KR102249009B1 (ko) * | 2020-08-31 | 2021-05-07 | 한정근 | 가연성 혼합폐기물과 생활폐기물 및 사업장폐기물 연료화 방법 |
KR102615764B1 (ko) * | 2021-09-09 | 2023-12-20 | 주식회사 에스피에너지 | 폐목재를 이용한 바이오 고형연료의 제조방법 |
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- 2014-06-09 US US15/124,062 patent/US10047312B2/en active Active
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KR20100078746A (ko) * | 2008-12-30 | 2010-07-08 | 코오롱건설주식회사 | 가연성 폐기물의 선별 분리 방법 및 가연성 폐기물의 에너지 연료화 방법 |
KR101091118B1 (ko) * | 2010-10-20 | 2011-12-09 | (주)대우건설 | 고형연료용 폐기물 전처리장치 |
KR101272172B1 (ko) * | 2011-11-30 | 2013-06-07 | 이상훈 | 알피에프 제조 시스템 |
KR20130076990A (ko) * | 2011-12-29 | 2013-07-09 | 코오롱글로벌 주식회사 | 폐기물 선별기 및 이것을 포함하는 고형재생연료 생산설비 및 생산방법 |
KR101270936B1 (ko) * | 2011-12-30 | 2013-06-11 | 한라산업개발 주식회사 | 이중 건조 시스템 및 이중 배가스 처리 시스템을 이용한 생활폐기물 및 매립폐기물의 고형연료 제조방법 |
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KR101574691B1 (ko) | 2015-12-04 |
KR20150104980A (ko) | 2015-09-16 |
US10047312B2 (en) | 2018-08-14 |
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