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KR890003931A - Continuous Carbonization Apparatus and Method - Google Patents

Continuous Carbonization Apparatus and Method Download PDF

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Publication number
KR890003931A
KR890003931A KR870009126A KR870009126A KR890003931A KR 890003931 A KR890003931 A KR 890003931A KR 870009126 A KR870009126 A KR 870009126A KR 870009126 A KR870009126 A KR 870009126A KR 890003931 A KR890003931 A KR 890003931A
Authority
KR
South Korea
Prior art keywords
cylinder
transfer screw
rotary furnace
gas
raw material
Prior art date
Application number
KR870009126A
Other languages
Korean (ko)
Other versions
KR900003885B1 (en
Inventor
김남형
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김남형
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Filing date
Publication date
Application filed by 김남형 filed Critical 김남형
Priority to KR1019870009126A priority Critical patent/KR900003885B1/en
Publication of KR890003931A publication Critical patent/KR890003931A/en
Application granted granted Critical
Publication of KR900003885B1 publication Critical patent/KR900003885B1/en

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Classifications

    • 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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/02—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used
    • C10G49/04—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used containing nickel, cobalt, chromium, molybdenum, or tungsten metals, or compounds thereof
    • 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
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Coke Industry (AREA)
  • Processing Of Solid Wastes (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

내용 없음No content

Description

부산물의 연속 탄화장치 및 방법Continuous Carbonization Apparatus and Method

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음As this is a public information case, the full text was not included.

제1도는 본 발명의 공정을 도시한 공정 개요도. 제2도는 본 발명의장치를 개략적으로 도시한 평면도, 제3도는 제2도는 A-A선에 대한 단면도.1 is a process schematic showing the process of the present invention. 2 is a plan view schematically showing the apparatus of the present invention, and FIG. 3 is a sectional view taken along line A-A.

Claims (2)

도시한 바와 같이 회전로(1)는, 이송스크류(5)를 보유하는 실린더(4)와, 환상연소실(2)의 양단측벽 및 분리실(3)측벽에 의해 지지되어 회전가능토록 설치된 각 회전부(6)(7)(8)(9)에는 일측면에 금속판(10)을 고정부착하고, 금속판(10)과 다른 금속판(11 )이 밀착되어 회전되게 압축스프링(12)을 탄력설치하여 기밀을 유지토록 설치하며, 상기 회전로(1)는 내면에 이송스클류판(13)을 다수개 고정부착하고, 외주출구단측에 기어(14)를 설치형성하되, 출구단의위치가 하방으로 약간의 경사도를 갖도록 설치하여, 모우터(15)에 연결설치된 피니언(16)에 의해 회전로(1)의 기러(14)가 맞물리어 회전가능토록 설치하며, 상기 이송스크류(5)를 보유하는 실린더(4)는 지지각(18)으로 고정지지된 호퍼(17)의 하방에 로타리밸브(19)와 연통되게 설치하여 모우터(20)의 구동에 의해 로타리밸브(19)와 이송스므류(5)가 회전가능토록 연결설치하며, 상기 환상연소실(2)은 하단측면에 유류 및 가스겸용버어너(21)를 가수개 설치하여 분리실(3)과 연통된 환류닥트(22)의 분기관(23)과 연통되게 설치하며, 상단에는 연도(24)를 설치하여 연소가스를 굴뚝으로 배출토록 하고, 연도(24)의 중간부에 설치딘 송풍기(26)를 보유하는 열교환기(25)와 원료공급부(27)가 연통되게 건조닥트(28)를 설치하며, 상기 분리실(3)은 하방의로타리밸브(29)와 연통되게 이송스크류(31)를 보유하는 실린더(30)를 설치하고, 실린더(30)의 외주에 냉각제와, 통과할 수 있도록 냉각실린더(32)를 설치 형성하되, 미도시의 모우터에 의해 로타리밸브(29)와 이송스크류(31)가 회전가능토록 연결설치된 부산물의 연속탄화 장치 및 방법.As shown in the drawing, the rotary furnace 1 is rotatably supported by the cylinder 4 holding the transfer screw 5 and the side walls of the annular combustion chamber 2 and the side wall of the separation chamber 3 so as to be rotatable. (6) (7) (8) (9) is fixedly attached to the metal plate 10 on one side, and the compression spring 12 is elastically installed so that the metal plate 10 and the other metal plate 11 are brought into close contact and rotated. The rotary furnace (1) is fixed to a plurality of transfer screw plate (13) on the inner surface, the gear 14 is installed on the outer outlet end side, but the position of the outlet end is slightly downward It is installed to have an inclination, the pinion 16 connected to the motor 15 is installed so that the girrel 14 of the rotary furnace 1 is rotatable and rotatable, and the cylinder holding the transfer screw ( 4) is installed in communication with the rotary valve 19 in the lower side of the hopper 17 fixed to the support angle (18) to rotate by the drive of the motor 20 The re-valve 19 and the transfer smear 5 are rotatably connected to each other, and the annular combustion chamber 2 is provided with a separate oil and gas burner 21 on the lower side thereof. It is installed in communication with the branch pipe 23 of the reflux duct 22, the flue 24 is installed at the top to discharge the combustion gas to the chimney, the blower installed in the middle of the flue (24) (26) The drying duct 28 is installed so that the heat exchanger 25 and the raw material supply part 27 which communicates with each other are in communication with each other, and the separation chamber 3 carries the transfer screw 31 in communication with the rotary valve 29 below. The cylinder 30 to be retained is installed, and a coolant and a cooling cylinder 32 are formed on the outer circumference of the cylinder 30 so as to pass therethrough, and the rotary valve 29 and the transfer screw ( 31) A continuous carbonization apparatus and method for byproducts rotatably connected. 식물의 잎, 줄기 또는 목재의 부산물등과 같이, 탄소를 다량함유한 유기물이나 석탄등의 원료, 즉 폐기물로 처리되는 부산물을 원료 공급부(27)에 건조한 다음 벨트컨베이어(34)를 이용하여 호퍼(17)에 투입하면 모우터 (20)에 의해 연결설치된 로타리밸브(19)와 실린더(4)의 이송스크류(5)에 의해 회전로 (1)로 이송된 부산물원료는 모우터(15)에 연결설치된 피니언(16)에 의해 회전로(1)의 기어 (14)가 맞물리어 회전됨에 따라 회전로 (1)내에서 부산물의 원료가 이송스크류(13)에 의해 서서히 이동되도록 함과 동시에, 회전로 (1)의 가열은 최소점화시 환상연소실(2)의 하단측면에 설치된 유류 및 가스겸용버어너(21)로 경유등과 같은 유류의 타에너지에 의존하고, 상기 가열에 의해 회전로(1)내에서 부산물의 원료가 이송스크류판(13)에 의해 출구단축으로 서서히이동되는 동안 탄화되면서 건류가스를 발생하고, 분리실(3)에서 탄소물질과 건류가스가 분리되며 발생된 건류가스의 일부는 환류닥트(22)의 중간에 설치된 송풍기(35)에 의해 회수하여 분리실(3)에서 환류닥트(22)와 각 분기관(23)을 통해유류 및 가스 겸용버어너(21)에 유입되어 환상의 연소실(2)에서 연소되고, 일부는 미도시의 폐열보일러에 의해 소각되어 굴뚝으로 배출되며, 상기 연소실(2)에서 연소된 연소가스는 열도(24)를 따라 굴뚝으로 배출되고 열도(24)의 중간부에 설치된 열교환기(25)에서 열교환되어 예열된공기는 송풍기(26)의 송풍력에 의해 건조닥트(28)를 따라 원료 공급부(27)를 통과하면서 원료를 건조시키며, 상기 분리실(3)에서 분리된 탄소물질은 미도시의 무우터에 의해 분리실(3)하방에 연통되게 설치된 로타리밸브(29)와 실린더(30)의이송스크류(31)에 의해 이송되는 동안 실린더(30)의 외주에 설치된 냉각실린더(32)내로 통과되는 냉각제에 의해 냉각된 탄소물질을 얻는 부산물의 연속탄화방법.Raw materials such as organic matter or coal containing carbon, i.e., by-products treated as waste, are dried in the raw material supply unit 27, such as the leaves, stems, or by-products of wood, and then the hopper (by using a belt conveyor 34). 17, the by-product material transferred to the rotary furnace (1) by the rotary valve 19 and the transfer screw (5) of the cylinder (4) installed by the motor 20 is connected to the motor (15). As the gear 14 of the rotary furnace 1 is engaged and rotated by the installed pinion 16, the raw material of the by-product in the rotary furnace 1 is gradually moved by the transfer screw 13, and at the same time, the rotary furnace The heating of (1) depends on other energy of oil such as light oil and the like with the oil and gas burner 21 installed on the lower end side of the annular combustion chamber 2 at the time of minimum ignition, and the rotary furnace 1 by the heating. The raw material of the by-product is gradually moved to the outlet shortening by the transfer screw plate 13 in the Carbonized gas is generated during carbonization, carbon material and dry gas are separated from the separation chamber 3, and a part of the generated dry gas is recovered by a blower 35 installed in the middle of the reflux duct 22 to separate the separation chamber. In (3), it flows into the oil and gas combined burner 21 through the reflux duct 22 and each branch pipe 23, and burns in the annular combustion chamber 2, and part of it is incinerated by a waste heat boiler (not shown). The exhaust gas is discharged to the chimney, and the combustion gas combusted in the combustion chamber 2 is discharged to the chimney along the archipelago 24 and heat-exchanged in the heat exchanger 25 installed in the middle of the archipelago 24 is a blower ( The raw material is dried while passing through the raw material supply unit 27 along the drying duct 28 by the blowing force of 26, and the carbon material separated from the separation chamber 3 is separated by a woofer not shown in the separation chamber 3. The transfer screw (31) of the rotary valve (29) and the cylinder (30) installed in communication with the lower part. A method of continuous carbonization of by-products obtained by cooling the carbon material by the coolant passed into the cooling cylinder 32 installed on the outer periphery of the cylinder (30) while being transported by). ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019870009126A 1987-08-20 1987-08-20 An apparatus and process for the continuing carbonization of by-product KR900003885B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019870009126A KR900003885B1 (en) 1987-08-20 1987-08-20 An apparatus and process for the continuing carbonization of by-product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1019870009126A KR900003885B1 (en) 1987-08-20 1987-08-20 An apparatus and process for the continuing carbonization of by-product

Publications (2)

Publication Number Publication Date
KR890003931A true KR890003931A (en) 1989-04-18
KR900003885B1 KR900003885B1 (en) 1990-06-04

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Application Number Title Priority Date Filing Date
KR1019870009126A KR900003885B1 (en) 1987-08-20 1987-08-20 An apparatus and process for the continuing carbonization of by-product

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100495236B1 (en) * 2002-06-12 2005-06-16 강병석 Cabonization equipment

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101218974B1 (en) * 2010-08-27 2013-01-07 주식회사 한성환경기연 Piston Pump

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100495236B1 (en) * 2002-06-12 2005-06-16 강병석 Cabonization equipment

Also Published As

Publication number Publication date
KR900003885B1 (en) 1990-06-04

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