WO2018151506A1 - Raffineur pour pyrolyseur - Google Patents

Raffineur pour pyrolyseur Download PDF

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Publication number
WO2018151506A1
WO2018151506A1 PCT/KR2018/001890 KR2018001890W WO2018151506A1 WO 2018151506 A1 WO2018151506 A1 WO 2018151506A1 KR 2018001890 W KR2018001890 W KR 2018001890W WO 2018151506 A1 WO2018151506 A1 WO 2018151506A1
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WO
WIPO (PCT)
Prior art keywords
exhaust gas
purifier
oil
refiner
water tank
Prior art date
Application number
PCT/KR2018/001890
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English (en)
Korean (ko)
Inventor
이달은
Original Assignee
이달은
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 이달은 filed Critical 이달은
Publication of WO2018151506A1 publication Critical patent/WO2018151506A1/fr

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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
    • 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
    • B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/002—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal in combination with oil conversion- or refining processes

Definitions

  • the present invention relates to a pyrolysis device configured to pyrolyze waste to obtain regenerated fuel, and more particularly, to recover foreign substances and oils including dust at a difference in specific gravity in exhaust gas discharged from pyrolysis of waste, and to clean the exhaust gas. It relates to a purifier for a pyrolysis device configured to discharge to the atmosphere.
  • an indirect heating pyrolysis apparatus for pyrolysis waste in a high temperature and vacuum environment includes a pyrolysis furnace including a pyrolysis furnace for pyrolyzing waste installed at an inside of a heating furnace, which is a heating means, at a high temperature and a vacuum state. And a refiner (oil collecting device) for collecting oil in the exhaust gas of the discharged waste.
  • FIG. 1 shows a schematic diagram of a conventional pyrolysis apparatus, and includes a pyrolyzer 1 and a refiner 2 for separating oil in exhaust gas discharged from the pyrolyzer 1.
  • the ordinary purifier 2 comprises a purifier tank 2a in which water is stored for cooling, and an exhaust gas guide tube 2b installed in the tank in a zigzag manner to guide the exhaust gas.
  • a 'U' shaped connector (2c) for cleaning is installed in the bending section of the exhaust gas guide pipe (2b) installed in a zigzag shape, and the inside of the pipe is periodically cleaned.
  • the efficiency is reduced due to the shutdown of the pyrolysis due to the cleaning.
  • the oil (Oil) contained in the exhaust gas is mixed with the foreign matter loaded in the tube has a disadvantage in that the recovery rate of the oil falls.
  • the present invention improves the recovery capacity of oil contained in the exhaust gas emitted from the pyrolysis device for pyrolyzing waste, and collects foreign substances such as dust contained in the exhaust gas to collect the exhaust gas discharged into the atmosphere.
  • An object of the present invention is to provide a purifier for a pyrolysis device, which is configured to reduce the amount of oil and foreign substances.
  • the present invention to achieve this object is, in the refiner for recovering oil from the exhaust gas discharged from the pyrolysis pyrolysis waste, a supply port to which the exhaust gas provided on one side is supplied, and is provided on the other side opposite to the supply port It includes a discharge port through which exhaust gas is discharged, an oil discharge port for discharging oil recovered on one side, and a foreign substance discharge port for discharging foreign substances deposited on the lower side, and the water is stored inside and divided into a water tank part and an exhaust gas passage part.
  • a hermetically sealed purifier body It is installed in the vertical direction in the upper side of the purifier body, and includes a plurality of moving passage diaphragm to form a zigzag-type exhaust gas movement path in the exhaust gas passage, while the lower end of the supply port for supplying the exhaust gas and
  • the lower end of the moving passage diaphragm may be located below the water surface of the water tank, so that the exhaust gas cannot be moved toward the lower end of the moving diaphragm.
  • One or more tank diaphragms are installed in the lower side of the refiner body to separate the tank into a plurality of unit tanks, and the upper end of the tank diaphragm is located at a position higher than the lower end of the movable diaphragm.
  • the pyrolytic purifier may further include a cooling water tank for cooling the purifier body using the cooling water.
  • a plurality of separation grooves in the vertical direction may be formed in the movable diaphragm.
  • the purifier for a pyrolyzer has a zigzag-type exhaust gas movement path formed in the exhaust gas passage part by a plurality of movement path diaphragms, so that the movement path of the exhaust gas becomes long, so that foreign substances in the exhaust gas are lowered.
  • the foreign matter falls to the provided water tank unit, and the foreign matter dropped into the water tank unit is not mixed back into the exhaust gas, thereby reducing the amount of foreign matter contained in the exhaust gas discharged to the atmosphere.
  • the exhaust gas is cooled by the cooling water tank to increase the efficiency of separating the oil and foreign matter and water contained in the exhaust gas.
  • FIG. 1 is a schematic diagram of a purifier for a pyrolysis machine in conventional use.
  • Figure 2 is a perspective schematic view of a purifier for an embodiment of the present invention pyrolysis.
  • Figure 3 is a schematic cross-sectional view of a purifier for a pyrolysis machine according to an embodiment of the present invention.
  • Figure 4 is a front sectional schematic view of a purifier for a pyrolysis machine according to one embodiment of the present invention.
  • Figure 5 is a side cross-sectional schematic view of a purifier for an pyrolysis machine according to one embodiment of the present invention.
  • Figure 6 is a detailed cross-sectional schematic view of the main part of the purifier for a pyrolysis machine which is one embodiment of the present invention.
  • Figure 7 is a perspective schematic view of the diaphragm for the movement of the purifier for a pyrolysis machine according to an embodiment of the present invention.
  • Figure 8 is a side cross-sectional schematic view of a purifier for a pyrolysis machine comprising a cooling bath which is another embodiment of the present invention.
  • Figure 9 is a perspective schematic view of a purifier for a pyrolysis machine comprising a cooling bath according to another embodiment of the present invention.
  • FIG. 10 is a side sectional schematic view of a purifier for a pyrolysis machine including a cooling bath according to another embodiment of the present invention shown in FIG. 9;
  • the present invention relates to a pyrolytic purifier for use in a pyrolysis device for pyrolyzing waste in a vacuum, high temperature state.
  • the present invention relates to a pyrolytic purifier configured to recover foreign substances and oil including dust at a difference in specific gravity in waste gas discharged from pyrolysis and discharge exhaust gas in a clean state to the atmosphere.
  • Such a refiner for a pyrolyzer includes a supply port through which exhaust gas is provided on one side, an exhaust port through which exhaust gas installed on the other side opposite to the supply port is discharged, an oil outlet through which oil recovered on one side is discharged, and
  • a hermetically sealed purifier body including a foreign substance discharge port for discharging the foreign substances precipitated on the side surface and having water stored therein and partitioned into a water tank part and an exhaust gas passage part; It is installed in the vertical direction in the upper side of the refiner body, and includes a plurality of moving passage diaphragm to form a zigzag-type exhaust gas passage in the exhaust gas passage portion,
  • the lower end of the supply port for supplying the exhaust gas and the lower end of the moving passage diaphragm are located below the water surface of the water tank so that the exhaust gas cannot move toward the lower end of the traveling diaphragm.
  • the configuration of the refiner 100 for the pyrolyzer according to the present invention includes a hermetically sealed purifier body 110 which is divided into a water tank unit 10 and an exhaust gas passage unit 20 by storing water therein; A plurality of moving plate plates 120 installed vertically on the upper side of the refiner body 110 to form a zigzag-type exhaust gas moving path in the exhaust gas passage part 20; It includes a configuration of one or more tank diaphragm 130 to separate the tank unit 10 formed in the lower side of the refiner body 110 into a plurality of unit tanks (11, 12, 13).
  • the purifier body 110 is connected to an exhaust gas guide tube for guiding the exhaust gas discharged from the pyrolyzer 1 and is provided with an exhaust gas supply port 111 formed at one side such that the exhaust gas is introduced therein, and the supply port ( 111 is installed on the other side opposite to the exhaust gas outlet 112 for discharging the exhaust gas from which oil and foreign substances have been removed, the oil outlet 113 for discharging the recovered oil on one side, and discharge the precipitated foreign matter It includes a foreign matter outlet 114.
  • the lower end 111a of the exhaust gas supply port 111 is positioned below the water surface of the water tank 10 so that the exhaust gas is discharged in the water tank. This can increase the cooling rate of the exhaust gas discharged to increase the collection efficiency of oil (Oil) and foreign matter.
  • the exhaust gas outlet 112 is connected to an exhaust gas guide tube that guides the exhaust gas to the flue so that the exhaust gas is discharged to the atmosphere through the flue.
  • the oil outlet 113 is configured to discharge the oil (Oil) collected on the water surface of the water tank unit 10 to the outside, located on the water surface of the water tank unit 10, as shown in Figure 4, is provided with a valve for opening and closing do.
  • the foreign matter discharge port 114 is configured to discharge the foreign matter precipitated in the water tank unit 10 to the outside, each foreign matter discharge port (114a, 114b, 114c) is installed in a plurality of unit tank (11, 12, 13) Each foreign matter discharge port (114a, 114b, 114c) is provided with an opening and closing valve.
  • the moving plate diaphragm 120 is configured to form a zigzag-type exhaust gas moving path in the exhaust gas passage part 20 as shown in FIG. 3, and the moving plate diaphragm 120 as shown in FIGS. 4 and 6.
  • the lower end 120a of the water tank 10 is positioned below the water surface so that the exhaust gas does not move through the lower end 120a of the moving plate diaphragm 120. That is, the exhaust gas is moved through the zigzag-shaped exhaust gas moving path.
  • the moving plate diaphragm 120 is installed in a vertical direction and is collected in a lower water tank unit 10 at the time of attachment of oil and foreign substances contained in the moving exhaust gas.
  • the moving plate diaphragm 120 may have a plurality of separation grooves 120b in the vertical direction to increase the collection efficiency of oil and foreign substances.
  • the plurality of separation grooves 120b interfere with the flow of the moving exhaust gas, so that oil and foreign substances are attached to the moving plate diaphragm 120 or fall downward. This phenomenon can increase the collection efficiency of oil and foreign matter.
  • the water tank diaphragm 130 is configured to separate the water tank unit 10 into a plurality of unit water tanks 11, 12, and 13, and the upper end 130a of the water tank diaphragm 130 is a movable diaphragm ( It is located at a position higher than the bottom (120a) of 120.
  • the water tank diaphragm 130 may be formed of one or more water tank diaphragms 131 and 132, and the unit water tanks 11, 12 and 13 formed by the plurality of water tank diaphragms 131 and 132 may be provided.
  • the water level is different.
  • the water level of the first water tank 11 positioned at the exhaust gas supply port 111 is set to be the highest, and the oil discharge port 113 is formed at the exhaust gas discharge port 112.
  • the oil collected in the second tank 13 is lower than the first tank diaphragm 131 so that the level of the second tank 13 is lower than that of the first tank diaphragm 131 so that the oil recovered as shown in FIG. 11 to the second tank 12, the third tank 13 to be moved.
  • the oil of the upper oil layer is discharged through the oil outlet 113, and the foreign matter of the lower sediment layer is discharged to the foreign material outlet 114 and recycled.
  • the cooling water tank 200 is configured such that the cooling water surrounds the entire purifier body 110. That is, the refiner body 110 is positioned in the cooling water tank 200 in which the cooling water is stored.
  • the cooling water tank 210 in which the coolant is stored is installed on the upper side of the refiner body 110, and the plurality of air-cooled cooling fins are provided on the side of the refiner body 110 and the cooling water tank 210. 220 is installed.
  • the air-cooled cooling fin 220 allows the refiner body 110 to be cooled by air-cooling, while cooling is performed by using the cooling water of the cooling water tank 210.
  • the pyrolytic purifier according to the present invention recovers foreign substances and oil containing dust at the difference in specific gravity in the exhaust gas discharged from pyrolysis, and discharges the clean exhaust gas to the atmosphere. Is expected.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Separating Particles In Gases By Inertia (AREA)

Abstract

La présente invention concerne un pyrolyseur configuré pour pyrolyser des déchets et pour acquérir du combustible régénéré et, plus particulièrement, un raffineur pour un pyrolyseur configuré pour récupérer des substances étrangères contenant de la poussière et de l'huile, en fonction d'une différence en termes de gravité spécifique, à l'intérieur du gaz d'échappement évacué pendant la pyrolyse des déchets, et pour évacuer le gaz d'échappement dans une état propre vers l'atmosphère. Un raffineur pour un pyrolyseur pour récupérer de l'huile à partir de gaz d'échappement déchargés à partir d'un pyrolyseur pour la pyrolyse de déchets selon la présente invention comporte: un corps de raffineur étanche comprenant une ouverture d'alimentation installée sur un côté de celui-ci pour fournir un gaz d'échappement, une ouverture d'évacuation installée sur l'autre côté opposé à l'ouverture d'alimentation pour évacuer le gaz d'échappement, une ouverture d'évacuation d'huile pour l'évacuation de l'huile récupérée sur une surface latérale, et une ouverture de décharge de substance étrangère pour l'évacuation des substances étrangères accumulées sur une surface inférieure, le corps de raffineur stockant de l'eau à l'intérieur de sorte que celui-ci est délimité en une partie de réservoir d'eau et une partie de passage de gaz d'échappement; et une pluralité de barrières de canal de transport installées verticalement sur le côté supérieur à l'intérieur du corps de raffineur de sorte qu'un canal de transport de gaz d'échappement est formé en zigzag dans la partie de passage de gaz d'échappement. L'extrémité inférieure de l'ouverture d'alimentation pour fournir un gaz d'échappement et les extrémités inférieures des barrières de canal de transport sont positionnées au-dessous de la surface d'eau dans la partie de réservoir d'eau de sorte que le gaz d'échappement ne se déplace pas vers les extrémités inférieures des barrières de canal de mouvement.
PCT/KR2018/001890 2017-02-14 2018-02-13 Raffineur pour pyrolyseur WO2018151506A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR10-2017-0019955 2017-02-14
KR1020170019955A KR101869333B1 (ko) 2017-02-14 2017-02-14 열분해기용 정제기

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Publication Number Publication Date
WO2018151506A1 true WO2018151506A1 (fr) 2018-08-23

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WO (1) WO2018151506A1 (fr)

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KR102556254B1 (ko) 2021-10-25 2023-07-18 유한회사 호원 오일포집을 위한 정제기와 이를 구비한 열분해처리장치
KR102611806B1 (ko) 2022-01-17 2023-12-11 유한회사 호원 열분해기용 콘덴서와 이를 구비한 열분해처리장치
KR20240013918A (ko) 2022-07-21 2024-01-31 주식회사 오투환경기술 열분해장치의 배기가스 처리시스템
KR102613920B1 (ko) 2023-04-13 2023-12-18 유한회사 호원 연속식 열분해 시스템

Citations (5)

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KR200330431Y1 (ko) * 2003-07-24 2003-10-17 천도철 유수 분리기
JP2008291076A (ja) * 2007-05-23 2008-12-04 Kayaba System Machinery Kk 炭素化装置
KR101334880B1 (ko) * 2013-01-09 2013-12-02 이달은 폐기물 처리시스템 및 그 시스템에 사용되는 배기가스 방지장치
KR20140145229A (ko) * 2013-06-12 2014-12-23 (주)그린필드 폴리염화비페닐이 함유된 폐절연유 연속공정식 처리장치 및 방법
JP2015209459A (ja) * 2014-04-24 2015-11-24 大谷開発株式会社 油化装置およびそれを備えた乾留式ガス化油化焼却システム

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KR100266852B1 (ko) 1998-06-22 2000-12-01 황해웅 화염 열분해 가스화 장치와, 이를 포함하는 화염 열분해 가스화및 저장 시스템
KR100513932B1 (ko) 2004-10-04 2005-09-09 한국기계연구원 용융 배가스를 열분해로내로 투입하여 폐기물을 직접 가열하는 열분해장치 및 이를 이용한 열분해 공정
KR100748624B1 (ko) 2006-11-16 2007-08-10 한국에너지기술연구원 로터리킬른형 열분해장치를 이용한 폐플라스틱의열분해시스템 및 그 방법
KR101379225B1 (ko) 2012-02-20 2014-04-04 이달은 열분해장치용 가스/오일 포집장치
KR101202810B1 (ko) 2012-02-20 2012-11-19 이달은 폐기물 열분해시스템

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR200330431Y1 (ko) * 2003-07-24 2003-10-17 천도철 유수 분리기
JP2008291076A (ja) * 2007-05-23 2008-12-04 Kayaba System Machinery Kk 炭素化装置
KR101334880B1 (ko) * 2013-01-09 2013-12-02 이달은 폐기물 처리시스템 및 그 시스템에 사용되는 배기가스 방지장치
KR20140145229A (ko) * 2013-06-12 2014-12-23 (주)그린필드 폴리염화비페닐이 함유된 폐절연유 연속공정식 처리장치 및 방법
JP2015209459A (ja) * 2014-04-24 2015-11-24 大谷開発株式会社 油化装置およびそれを備えた乾留式ガス化油化焼却システム

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