KR900003885B1 - An apparatus and process for the continuing carbonization of by-product - Google Patents

An apparatus and process for the continuing carbonization of by-product Download PDF

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KR900003885B1
KR900003885B1 KR1019870009126A KR870009126A KR900003885B1 KR 900003885 B1 KR900003885 B1 KR 900003885B1 KR 1019870009126 A KR1019870009126 A KR 1019870009126A KR 870009126 A KR870009126 A KR 870009126A KR 900003885 B1 KR900003885 B1 KR 900003885B1
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cylinder
transfer screw
rotary furnace
raw material
gas
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KR1019870009126A
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KR890003931A (en
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김남형
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김남형
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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
    • 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

A superior carbon material is manufactured by using a dry distillation gas produced in the carbonization of an organic matter or charcoal. The organic matter contains a large quantity of carbon and is pref. leaves and stalks of plant, and byproducts of wood. The continuous carbonization apparatus comprises a feeder of raw material, a rotary furnace, a transfer screw, a circular combustion chamber, a separating chamber, a heat exchanger and a drying duct.

Description

부산물의 연속 탄화장치 및 방법Continuous Carbonization Apparatus and Method

제 1 도는 본 발명의 공정을 도시한 공정개요도.1 is a process overview showing the process of the present invention.

제 2 도는 본 발명의 장치를 개략적으로 도시한 평면도.2 is a plan view schematically showing the apparatus of the present invention.

제 3 도는 제 2 도의 A-A선에 대한 단면도.3 is a cross-sectional view taken along the line A-A of FIG.

제 4 도는 제 2 도의 B-B선에 대한 단면도.4 is a sectional view taken along line B-B in FIG.

제 5 도는 제 2 도의 "A"부에 대한 확대 단면도.5 is an enlarged cross-sectional view of the portion "A" of FIG.

* 도면의 주요부분에 대한 부호의 설명* Explanation of symbols for main parts of the drawings

1 : 회전로 2 : 연소실1: rotary furnace 2: combustion chamber

3 : 분리실 4,30 : 실린더3: separation chamber 4,30: cylinder

5,31 : 이송스크류 6,7,8,9 : 회전부5,31: Transfer screw 6,7,8,9: Rotating part

10,11 : 금속판 12 : 압축스프링10,11 metal plate 12 compression spring

13 : 이송스크류판 14 : 기어13: transfer screw plate 14: gear

15,20 : 모우터 16 : 피니언15,20: motor 16: pinion

17 : 호퍼 18 : 지지각17: Hopper 18: support angle

19,29 : 로타리 밸브 21 : 유류및 가스겸용버어너19,29: Rotary valve 21: Combined oil and gas burner

22 : 환류덕트 23 : 분기관22: reflux duct 23: branch pipe

24 : 연도 25 : 열교환기24: year 25: heat exchanger

26 : 송풍기 27 : 원료공급부26: blower 27: raw material supply unit

28 : 건조닥트 32 : 냉각실린더28: dry Doc 32: cooling cylinder

본 발명은 거의 다른 연료에 의존함이 없이, 식물의 잎, 줄기 또는 목재의 부산물 등과 같이 탄소를 다량 함유한 유기물이나 석탄 등의 원료탄화시에 발생되는 건류가스를 연소시켜 상기 건류가스의 연소열만으로 양질의 탄소물질을 제조할 수 있도록 된 부산물의 연소탄화장치 및 방법에 관한 것이다.The present invention does not depend on almost any other fuel, and burns dry gas generated during carbonization of raw materials such as organic matter or coal containing a large amount of carbon, such as by-products of plants, leaves, stems, or wood. The present invention relates to a combustion carbonization apparatus and method for producing by-products of high quality carbon material.

종래 부산물의 탄화장치는 건류가스에 의존치 않고 타연료의 연소열에 의하여 식물의 잎, 줄기나 목재의 부산물 등과 같이 탄소를 다량 함유한 유기물이나 석탄등의 원료를 탄화토록 된 것인바, 탄소물질의 질이 낮아 화목, 목탄 등과 같이 숯을 만드는 정도에 불과하고, 공업적으로 양산이 곤란하며, 특히 건류가스가 아닌 타연료의 연소열에 의존하므로, 극히 채산성이 낮은 것이었다.Conventional carbonation equipment of by-products is to rely on carbonaceous materials such as organic matter or coal, which contain a large amount of carbon such as by-products of plants, leaves, stems, and wood by the combustion heat of other fuels. The quality is low enough to make charcoal such as firewood and charcoal, and it is difficult to mass produce industrially. In particular, it is extremely low in profitability because it depends on the heat of combustion of fuel other than dry gas.

본 발명은 이러한 종래의 제반폐단 및 문제점을 해결하기 위한 것으로, 초기 점화하여 건류가스발생시까지 타연료를 사용하고, 건류가스의 발생후에는 원료의 탄화시에 발생되는 건류가스를 연소케하여 원료자체에서 발생되는 건류가스의 연소열만으로 연속가열이 가능하게된 것이어서, 타연료에 의존함이 거의 없이 양질의 탄소물질을 경제적으로 양산할 수 있어, 염가로 제공할 수 있을뿐만 아니라, 에너지의 절감에도 크게이바지할 수 있는 부산물의 연속탄화장치 및 방법을 제공하는데 그 주요목적이 있다.The present invention is to solve such a conventional closure and problems, using other fuel until the initial ignition and dry gas generation, and after the generation of dry gas, the dry gas generated during the carbonization of the raw material to burn the raw material itself Continuous heating is possible only by the combustion heat of dry gas generated from the gas, so it is possible to economically mass-produce high-quality carbon materials with little dependence on other fuels. Its main purpose is to provide a continuous carbonization apparatus and method which can contribute.

이하 본 발명을 첨부된 도면에 의거 상세하게 설명하면 다음과 같다. 도시한 바와같이, 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 설치한다.Hereinafter, the present invention will be described in detail with reference to the accompanying drawings. As shown in the drawing, the rotary furnace 1 is supported by the cylinder 4 holding the transfer screw 5 and the side walls of the annular combustion chamber 2 and the side walls 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 with each other to ensure airtightness. Install to maintain.

상기 회전로(1)는 내면에 이송스크류판(13)을 다수개 고정부착하고, 외주출구단측에 기어(14)를 설치형성하되, 출구단의 위치가 하방으로 약간의 경사도를 갖도록 설치하여, 모우터(15)에 연결설치된 피니언(16)에 의해 회전로(1)의 기어(14)가 맞물리어 회전가능토록 설치하고, 회전로(1)의 회전은 3-20R.P.M범위내에서 회전조절이 가능하게 한다.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 outlet end is installed to have a slight inclination downward, The pinion 16 connected to the motor 15 is installed so that the gear 14 of the rotary furnace 1 can rotate and rotate, and the rotation of the rotary furnace 1 rotates within the range of 3-20 R.PM. Make adjustments possible.

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 이송스크류(5)가 회전가능토록 연결설치한다.The cylinder (4) holding the transfer screw (5) is installed in communication with the rotary valve (19) below the hopper (17), which is fixed at the support angle (18) to drive the rotary by the motor 20 The valve 19 and the transfer screw 5 are rotatably installed.

상기 환상연소실(2)은 하단측면에 유류 및 가스겸용 버어너(21)를 다수개 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 설치된 송풍기(26)를 보유하는 열교환기(25)와 원료공급부(27)가 연통되게 건조닥트(28)를 설치한다.The annular combustion chamber (2) is installed in communication with the branch pipe 23 of the reflux duct (22) in communication with the separation chamber 3 by installing a plurality of burner (21) for oil and gas on the lower side, In order to discharge flue gas to the chimney by installing a flue 24, a heat exchanger 25 having a blower 26 installed in the middle of the flue 24 and a raw material supply unit 27 communicate with each other. 28) install.

상기 분리실(3)은 하방의 로타리밸브(29)와 연통되게 이송스크류(31)를 보유하는 실린더(30)를 설치하고, 실린더(30)의 외주에 냉각제가 통과할 수 있도록 냉각실린더(32)를 설치형성하여, 미도시의 모우터에 의해 로타리밸브(29)와 이송스크류(31) 가 회전가능토록 연결설치한다.The separation chamber (3) is provided with a cylinder (30) holding a transfer screw (31) in communication with the lower rotary valve (29), the cooling cylinder 32 so that the coolant can pass through the outer periphery of the cylinder (30) ), And the rotary valve 29 and the transfer screw 31 are rotatably connected by a motor (not shown).

도면중 미설명부호 34는 벨트컨베이어, 35는 환류닥트(22)의 송풍기이다. 이와같이 구성된 본 발명은, 먼저 식물의 잎, 줄기 또는 목재의 부산물 등과같이, 탄소를 다량 함유한 유기물이나, 석탄등의 원료 즉, 폐기물로 처리되는 부산물을 원료공급부(27)에서 건조한 다음, 벨트컨베이어(34)를 이용하여 호퍼(17)에 투입하면, 모우터(20)에 연결설치된 로타리밸브(19)와 실린더(4)의 이송스크류(5)에 의해 회전로(1)로 이송된다.In the figure, reference numeral 34 denotes a belt conveyor, and 35 denotes a blower of the reflux duct 22. According to the present invention configured as described above, first, organic materials containing a large amount of carbon, such as by-products of leaves, stems, or wood, or by-products such as coal, which are processed as wastes, are dried in the raw material supply unit 27, and then a belt conveyor is used. When the hopper 17 is inserted into the hopper 17, the rotary valve 1 is connected to the rotary furnace 1 by the rotary valve 19 connected to the motor 20 and the transfer screw 5 of the cylinder 4.

회전로(1)에 이송된 부산물원료는, 모우터(15)에 연결설치된 피니언(16)에 의해 회전로(1)의 기어(14)가 맞물리어 회전하게 되고, 회전로(1)의 회전은 3-20R.P.M범위내에서 회전조절이 가능토록 설치하는 것이 바람직하다. 그 이유는, 부산물의 원료에 따라서 탄화도 및 생산량을 조절함으로서, 양질의 탄소물질을 얻기 위함이다.The by-product raw material transferred to the rotary furnace 1 is rotated by the gear 14 of the rotary furnace 1 is engaged by the pinion 16 connected to the motor 15, the rotation of the rotary furnace 1 Silver should be installed to allow rotation control within the range of 3-20 R.PM. The reason for this is to obtain high quality carbon material by adjusting the degree of carbonization and the production amount according to the raw material of the by-product.

회전로(1)의 가열은 최초점화시, 환상연소실(2)의 하단측면에 설치된 유류 및 가스겸용 버어너(21)로 경유등과 같은 유류의 타에너지에 의존한다.The heating of the rotary furnace 1 depends on the other energy of the oil, such as light oil and the like, in the oil and gas burner 21 installed on the lower end side of the annular combustion chamber 2 at the time of initial ignition.

상기 가열에 의해 회전로(1)내에서 부산물의 원료가 이송스크류판(13)에 의해 서서히 이송되는동안 탄화되면서 건류가스를 발생하고, 회전로(1) 단부의 분리실(3)에서 탄소물질과 건류가스가 분리된다. 원료의 탄화시 발생된 일부의 건류가스는, 환류닥트(22)의 중간에 설치된 송풍기(35)에 의해 분리실(3)에서 환류닥트(22)와 각 분기판(23)을 통해 유류 및 가스겸용 버어너(21)에 유입되어 환상의 연소실(2)에서 연소되며, 일부는 미도시의 폐열보일러에 의해 소각되어 굴뚝으로 배출된다.By heating, carbonaceous material is generated while carbonized while the raw material of the by-product is slowly transported by the transfer screw plate 13 in the rotary furnace 1, and the carbon material in the separation chamber 3 at the end of the rotary furnace 1 And dry gas are separated. Some of the dry gas generated during the carbonization of the raw material is oil and gas through the reflux duct 22 and each branch plate 23 in the separation chamber 3 by the blower 35 installed in the middle of the reflux duct 22. It is introduced into the combined burner 21 and burned in the annular combustion chamber 2, and part of it is incinerated by a waste heat boiler (not shown) and discharged into the chimney.

그리고, 연소실(2)에서 연소된 연소가스는 연도(24)를 따라 굴뚝으로 배출되고, 연도(24)의 중간부에 설치된 열교환기(25)에서 열교환되어 예열된 공기는 송풍기(26)의 송풍력에 의해 건조닥트(28)를 따라 원료공급부(27)를 통과하면서 원료를 건조시키다.The combustion gas combusted in the combustion chamber 2 is discharged to the chimney along the flue 24, and the air preheated by being heat-exchanged in the heat exchanger 25 installed in the middle of the flue 24 is transferred to the blower 26. The raw material is dried while passing the raw material supply part 27 along the drying duct 28 by the wind power.

상기 분리실(3)에서 분리된 탄소물질은, 미도시의 모우터에 의해 분리실(3) 하방에 연통되게 설치된 로타리밸브(29)와 실린더(30)의 이송스크류(31)에 의해 이송되는 동안 실린더(30)의 외주에 설치된 냉각실린더(32)내로 통과되는 냉각제에 의해 냉각된 양질의 탄소물질을 얻는다.The carbon material separated from the separation chamber 3 is transferred by a rotary valve 29 and a transfer screw 31 of the cylinder 30 installed to communicate under the separation chamber 3 by a motor (not shown). While the high quality carbon material cooled by the coolant passed into the cooling cylinder 32 installed on the outer periphery of the cylinder 30 is obtained.

상술한 바와같이 본 발명에 의하면, 식물의 잎, 줄기 또는 목재의 부산물 등과 같이 탄소를 다량 함유한 유기물이나 석탄, 즉 식물성 부산물의 원료를 회전로(1)내에 투입시켜 부산물원료의 자체에서 발생되는 건류가스에 의한 연소열만으로 연속탄화작업이 가능하므로 양질의 탄소물질을 양산할 수 있어, 염가로 제공할 수 있을뿐만 아니라, 에너지의 절감에도 크게 이바지할 수 있는 산업상 유용한 발명인 것이다.As described above, according to the present invention, organic materials or coals containing a large amount of carbon, such as by-products of plants, leaves or stems, or wood, that is, vegetable by-products are introduced into the rotary furnace 1 to generate the by-products. Since the continuous carbonization operation is possible only by the heat of dry gas, it is possible to mass-produce high-quality carbon materials, which can be provided at low cost, and is an industrially useful invention that can greatly contribute to energy saving.

Claims (2)

도시한 바와같이 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 이송스크류판(13)을 다수개 고정부착하고, 외주출구단측에 기어(14)를 설치형성하되, 출구단의 위치가 하방으로 약간의 경사도를 갖도록 설치하여, 모우터(15)에 연결설치된 피니언(16)에 의해 회전로(1)의 기어(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 이송스크류(5)가 회전가능토록 연결설치하며, 상기 환상연소실(2)은 하단측면에 유류 및 가스겸용버어너(21)를 다수개 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 설치된 송풍기(26)를 보유하는 열교환기(25)와 원료공급부(27)가 연통되게 건조닥트(28)를 설치하며, 상기 분리실(3)은 하방의 로타리밸브(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 연속탄화장치 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) fixedly attaches the metal plate 10 to one side, and elastically installs the compression spring 12 so that the metal plate 10 and the other metal plate 11 come into close contact and are 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 peripheral 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 gear 14 of the rotary furnace 1 is rotatable and rotatable, the cylinder holding the conveying screw ( 4) is installed in communication with the rotary valve 19 under the hopper 17 fixed to the support angle (18) by the drive of the motor 20 The revalve 19 and the transfer screw 5 are rotatably connected to each other, and the annular combustion chamber 2 communicates with the separation chamber 3 by installing a plurality of oil and gas burners 21 on the lower side. 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, and the blower 26 installed in the middle of the flue (24) The drying duct 28 is installed so that the heat exchanger 25 and the raw material supply unit 27 communicate with each other, and the separation chamber 3 holds the transfer screw 31 in communication with the rotary valve 29 below. The cylinder 30 is installed, and the cooling cylinder 32 is installed and formed so as to pass through the coolant on the outer circumference of the cylinder 30, but the rotary valve 29 and the transfer screw 31 are formed by a motor (not shown). Apparatus and method for continuous carbonization of rotatable by-products. 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 최초점화시 환상연소실(2)의 하단측면에 설치된 유류 및 가스겸용버어너(21)로 경유등과 같은 유류의 타에너지에 의존하고, 상기 가열에 의해 회전로(1)내에서 부산물의 원료가 이송스크류관(13)에 의해 출구단측으로 서서히 이동되는 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 통해 유류 및 가스겸용버어너(21)에 유입되어 환상의 연소실(2)에서 연소되고, 일부는 미도시의 폐열보일러에 의해 소각되어 굴뚝으로 배출되며, 상기 연소실(2)에서 연소된 연소가스는 연도(24)를 따라 굴뚝으로 배출되고 연도(24)의 중간부에 설치된 열교환기(25)에서 열교환되어 예열된 공기는 송풍기(26)의 송풍력에 의해 건조닥트(28)를 따라 원료공급부(27)를 통과하면서 원료를 건조시키며, 상기 분리실(3)에서 분리된 탄소물질은 미도시의 모우터에 의해 분리실(3) 하방에 연통되게 설치된 로타리밸브(29)와 실린더(30)의 이송스크류(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 connected by the motor 20 is connected to the motor 15. As the gear 14 of the rotary furnace 1 is 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 the other energy of oil such as light oil by the oil and gas combined burner 21 installed on the lower end side of the annular combustion chamber 2 at the time of initial ignition, and the rotary furnace 1 by the heating. Raw material of the by-product is gradually moved to the outlet end side by the transfer screw pipe 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 ( 3) flows into the oil and gas combined burner 21 through the reflux duct 22 and each branch pipe 23 and is burned in the annular combustion chamber 2, and part 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 flue 24 and heat-exchanged in the heat exchanger 25 installed in the middle of the flue 24 is blower 26 The raw material is dried while passing through the raw material supply unit 27 along the drying duct 28 by the blowing force of), and the carbon material separated from the separation chamber 3 is separated by a motor (not shown). Feeding screw 31 of the rotary valve 29 and the cylinder 30 installed in communication with the lower side Continuous carbonization method of the by-products to obtain a carbon material cooled by the coolant that is passed into the cooling cylinder 32 provided on the outer periphery of the cylinder 30 while being conveyed by.
KR1019870009126A 1987-08-20 1987-08-20 An apparatus and process for the continuing carbonization of by-product KR900003885B1 (en)

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KR101218974B1 (en) * 2010-08-27 2013-01-07 주식회사 한성환경기연 Piston Pump

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KR100495236B1 (en) * 2002-06-12 2005-06-16 강병석 Cabonization equipment

Cited By (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

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