KR100465151B1 - A carbonization system - Google Patents

A carbonization system Download PDF

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Publication number
KR100465151B1
KR100465151B1 KR1020040041801A KR20040041801A KR100465151B1 KR 100465151 B1 KR100465151 B1 KR 100465151B1 KR 1020040041801 A KR1020040041801 A KR 1020040041801A KR 20040041801 A KR20040041801 A KR 20040041801A KR 100465151 B1 KR100465151 B1 KR 100465151B1
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KR
South Korea
Prior art keywords
organic material
organic
conveyor
heat
carbonization
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KR1020040041801A
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Korean (ko)
Inventor
박흥원
최삼룡
이종래
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주식회사 아이이아이
주식회사 오리콘
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Priority to KR1020040041801A priority Critical patent/KR100465151B1/en
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Publication of KR100465151B1 publication Critical patent/KR100465151B1/en

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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/20—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having rotating or oscillating drums
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/033—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment comminuting or crushing
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/04—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00—Pretreatment
    • F23G2201/10—Drying by heat
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2203/00—Furnace arrangements
    • F23G2203/80—Furnaces with other means for moving the waste through the combustion zone
    • F23G2203/801—Furnaces with other means for moving the waste through the combustion zone using conveyors
    • F23G2203/8013—Screw conveyors

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Treatment Of Sludge (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

PURPOSE: A continuous organic matter carbonization kiln is provided to discharge carbonized matters by drying, carbonizing and cooling organic matters through a nozzle with a rapid cooler, and to recycle carbonized matters as dewatering agent, cover materials, fuel, soil conditioner and active carbon. CONSTITUTION: A continuous organic matter carbonization kiln system comprises a mixer(100) having a hopper(110) inputting organic matters to be carbonized, a cutter(120) placed in the lower part of the hopper to crush organic matters and a screw(130) mixing and moving crushed organic matters to a discharge port(140), a drier(300) directly heating organic matters at temperature of 250 deg.C through the discharge port of the screw by a first conveyor(200) and moving dry organic matters to a second conveyor(400), a carbonization kiln(500) indirectly heating, drying and carbonizing organic matters at temperature of 600 to 900 deg.C from the drier by the second conveyor, and a stabilizing kiln(600) manufacturing active carbon by receiving organic matters from the carbonization kiln.

Description

연속식 유기물 탄화로 시스템{A carbonization system}Continuous Organic Carbonization System {A carbonization system}

본 발명은 연속식 유기물 탄화로 시스템에 관한 것으로, 특히 일반쓰레기, 협잡물, 음식물쓰레기, 하수슬러지등과 같은 유기물을 건조 탄화처리 하고 탄화된 탄화물은 사용 목적에 따라 탈수보조제, 복토, 연료화, 토양개선제, 활성탄 제조원료로 재활용할 수 있도록 한 연속식 유기물 탄화로 시스템에 관한 것이다.The present invention relates to a continuous organic carbonization furnace system, in particular dry carbonization of organic matter, such as general waste, contaminants, food waste, sewage sludge, and carbonized carbide dehydration aid, cover, fuelization, soil improver according to the purpose of use The present invention relates to a continuous organic carbonization system that can be recycled as an activated carbon manufacturing material.

일반적으로 일반 생활쓰레기, 및 협잡물, 음식물쓰레기, 하수슬러지등과 같은 유기물은 무기물에 비하여 수분함량이 높으며, 이러한 유기물은 소각시 다량의 환경오물질이 발생되고, 소각된 잔재물을 별도로 처리해야 하는 제반 문제점이 발생되었다.In general, organic matters such as general household waste, and trash, food waste, sewage sludge, etc., have higher moisture content than inorganic ones, and these organic matters generate a large amount of environmental pollutants and incineration residues must be treated separately. A problem has occurred.

따라서 본 발명의 목적은 상기와 같은 종래의 문제점을 감안하여 안출한 것으로, 일반쓰레기, 협잡물, 음식물쓰레기, 하수슬러지등과 같은 유기물을 건조 탄화처리 하고 탄화된 탄화물은 사용 목적에 따라 탈수보조제, 복토, 연료화, 토양개선제, 활성탄 제조원료로 재활용할 수 있도록 한 연속식 유기물 탄화로 시스템을 제공하는데 있다.Therefore, the object of the present invention is devised in view of the above-described conventional problems, dry carbonization of organic matters such as general garbage, contaminants, food waste, sewage sludge and carbonized carbide dehydration aid, cover It is to provide a continuous organic carbonization system that can be recycled as fuel, fuel, soil improver and activated carbon.

도1은 본 발명에 따른 유기물 탄화로 시스템을 나타낸 구성도,1 is a block diagram showing an organic carbonization furnace system according to the present invention,

도2는 본 발명에 따른 탄화로의 정면도,2 is a front view of a carbonization furnace according to the present invention;

도3는 본 발명에 따른 건조기의 정면도,3 is a front view of a dryer according to the present invention;

도4는 본 발명에 따른 탄화로의 정면도.4 is a front view of a carbonization furnace according to the present invention.

(도면중 주요 부분에 대한 부호의 설명)(Explanation of symbols for the main parts of the drawing)

100 ; 믹서기 200 ; 제1컨베이어100; Mixer 200; 1st Conveyor

300 ; 건조기 400 ; 제2컨베이어300; Dryer 400; 2nd Conveyor

500 ; 탄화로 600 ; 안정화로500; Carbonization furnace 600; Stabilization furnace

상기와 같은 목적을 달성하기 위한 수단으로 본 발명은, 탄화하고자 하는 유기물이 투입되는 호퍼와;As a means for achieving the above object, the present invention, the organic material to be carbonized hopper;

상기 호퍼 하단에 위치하고 투입되는 유기물을 일정한 크기로 분쇄하는 커터기가 내부 상단에 형성되며, 이 커터기 하단에는 일정 크기로 분쇄된 유기물이 낙하되면 유기물을 믹싱시키면서 배출구로 이동시키는 스크류가 구비되는 믹서기와;A mixer having a cutter positioned at a lower end of the hopper to grind the organic material into a predetermined size is formed at an upper end thereof, and a mixer having a screw to move to an outlet while mixing the organic material when the organic material dropped to a predetermined size falls;

상기 스크류의 배출구를 통과한 유기물이 제1컨베이어에 의해 내부로 투입되면 100~250℃의 고온으로 직접 가열 건조시키고 건조된 유기물은 제2컨베이어측으로 이동시키는 건조기와;When the organic material passing through the discharge port of the screw is introduced into the interior by the first conveyor is directly heated to dry at a high temperature of 100 ~ 250 ℃ and the dried organic material is moved to the second conveyor side;

상기 건조기를 통과한 유기물이 제2컨베이어에 의해 내부로 투입되면 다시 유기물을600~900℃의 고온에서 간접 가열 건조시켜 탄화시키는 탄화로와;A carbonization furnace in which the organic material having passed through the dryer is introduced into the interior by a second conveyor, and carbonized by indirectly heating and drying the organic material at a high temperature of 600 to 900 ° C. again;

상기 탄화로를 통과한 유기물이 내부로 투입되면 이를 활성탄으로 제조되게 하는 안정화로로 구성되는 것을 그 기술적 구성상의 기본 특징으로 한다.When the organic material passed through the carbonization furnace is introduced into the stabilization furnace to be made into activated carbon as a basic feature of the technical configuration.

이하 본 발명의 바람직한 실시예를 첨부도면을 참조하여 보다 상세하게 설명하면 다음과 같다.Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.

도1은 본 발명에 따른 유기물 탄화로 시스템을 나타낸 구성도 이고, 도2는 본 발명에 따른 탄화로의 정면도 이며, 도3는 본 발명에 따른 건조기의 정면도 이며, 도4는 본 발명에 따른 탄화로의 정면도이다.1 is a configuration diagram showing an organic carbonization furnace system according to the present invention, Figure 2 is a front view of a carbonization furnace according to the present invention, Figure 3 is a front view of a dryer according to the present invention, Figure 4 is a present invention The front view of the carbonization furnace along.

본 발명은 도1 내지 도4에서와 같이 탄화하고자 하는 유기물이 투입되는 호퍼(110)와, 상기 호퍼(110) 하단에 위치하고 투입되는 유기물을 일정한 크기로 분쇄하는 커터기(120)가 내부 상단에 형성되며 이 커터기(120) 하단에는 일정 크기로 분쇄된 유기물이 낙하되면 유기물을 믹싱시키면서 배출구(140)로 이동시키는 스크류(130)가 구비되는 믹서기(100)와, 상기 스크류(130)의 배출구(140)를 통과한 유기물이 제1컨베이어(200)에 의해 내부로 투입되면 250℃의 고온으로 직접 가열 건조시키고 건조된 유기물은 제2컨베이어(400)측으로 이동시키는 건조기(300)와, 상기 건조기(300)를 통과한 유기물이 제2컨베이어(400)에 의해 내부로 투입되면 다시 유기물을 600~900℃의 고온에서 간접 가열 건조시켜 탄화시키는 탄화로(500))와, 상기 탄화로(500)를 통과한 유기물이 내부로 투입되면 이를 활성탄으로 제조되게 하는 안정화로(600)로 구성된다.In the present invention, as shown in Figs. 1 to 4, the hopper 110 into which the organic material to be carbonized is introduced, and the cutter 120 for crushing the organic material placed in the bottom of the hopper 110 into a predetermined size is formed at the upper end thereof. At the bottom of the cutter 120, when the organic material pulverized to a predetermined size falls, the mixer 100 having a screw 130 moving to the outlet 140 while mixing the organic material and the outlet 140 of the screw 130 are provided. When the organic material having passed through) is introduced into the inside by the first conveyor 200, the dryer is directly heated and dried at a high temperature of 250 ° C., and the dried organic material is moved to the second conveyor 400, and the dryer 300. When the organic material passed through) is introduced into the inside by the second conveyor 400, the organic material is indirectly heated and dried by carbonization at a high temperature of 600 to 900 ° C.) and through the carbonization furnace 500. An organic substance thrown into the interior When it is configured as a stabilization of the activated carbon to be prepared (600).

건조기(300)의 일단에는 열풍발생장치로 부터 열이 공급되는 열공급통로(320)가 형성되고 타단에는 제1컨베이어(200)에 의해 이송된 유기물이내부로 투입되게 하는 투입구(330)가 각각 형성되는 본체(310)와, 상기 열공급통로(320)와 투입구(330) 사이에 회전될 수 있도록 설치되고 내부로 열이 공급되면 구동부(340)에 의해 회전하면서 유기물을 직접 가열시키는 회전가열통(350)과, 상기 회전가열통(350) 내부에 위치하고 유기물이 골고루 건조되게 하면서 제2컨베이어(400)측으로 이송되게 하는 로터리 스크류(360)로 구성된다.At one end of the dryer 300, a heat supply passage 320 for supplying heat from the hot air generator is formed, and at the other end, an inlet 330 is formed to allow the organic material transferred by the first conveyor 200 to be introduced therein. It is installed so as to be rotated between the main body 310 and the heat supply passage 320 and the inlet 330, when the heat is supplied into the rotary heating tube 350 to directly heat the organic material while rotating by the drive unit 340 And a rotary screw 360 positioned in the rotary heating tube 350 to be transported to the second conveyor 400 while the organic material is evenly dried.

탄화로(500)의 일단 상부에는 제2컨베이어(400)에 의해 이송된 유기물이 내부로 투입되게 하는 투입구(510)가 형성되고 타단 저면에는 건조된 유기물이 아래 방향으로 배출되게 하는 배출구(520)가 일체로 형성되는 케이싱(530)과, 상기 케이싱(530) 내부에 장치되고 투입된 유기물을 일방향으로 이송시키는 회전스크류(540)와, 상기 케이싱(530) 몸체를 밀실하게 차단하며 열풍발생장치로 부터 발생된 열이 내부로 유입되면 간접 가열시킬 수 있도록 일단에는 열유입구(560)가 형성되고 타단에는 건조하면서 발생된 가스를 외부로 배출되게 하는 가스배출구(570)를 갖는 간접가열통(550)으로 구성된다.An inlet 510 is formed at one end of the carbonization furnace 500 to allow the organic material transported by the second conveyor 400 to be introduced therein, and at the bottom of the other end, the outlet 520 for discharging the dried organic material downward. The casing 530 is formed integrally with, the rotating screw 540 for conveying the organic material introduced into the casing 530 in one direction and the casing 530 body tightly shut off from the hot air generating device The heat inlet 560 is formed at one end so that the generated heat is indirectly heated when introduced into the inside, and the indirect heating tube 550 having a gas outlet 570 for discharging the generated gas to the outside at the other end. It is composed.

안정화로(600)는 탄화로(500)의 배출구(520)와 연결되는 투입구(610)가 상단에 형성되고 내부에 회전스크류(630)가 장치되는 케이싱(620)과, 상기 회전스크류(630)의 끝단에 연결 설치되어 회전스크류(630)를 따라 이송된 유기물을 급속냉각기(650)로 보내는 노즐(640)과, 상기 케이싱(620) 외부를 밀실하게 감싸 열을 내부로 공급케 하여 유기물을 탄화할 수 있도록 한쪽에는 열유입구(660)가 형성되고 타단에서 열배출구(670)가 형성되는 안정화통(680)으로 구성된다.Stabilization furnace 600 is a casing 620 and the rotating screw 630 is provided with an inlet 610 connected to the outlet 520 of the carbonization furnace 500 is formed at the top and the rotating screw 630 therein, It is connected to the end of the nozzle 640 to send the organic material transported along the rotating screw 630 to the rapid cooler 650, and the casing 620 is tightly wrapped to supply heat to the inside to carbonize the organic material The heat inlet 660 is formed on one side so that the heat discharge port 670 is formed at the other end is composed of a stabilization cylinder 680.

이와 같이 구성된 본 발명은 최초 탄화하고자 하는 유기물 즉, 일반 생활쓰레기, 협잡물, 음식물찌꺼기, 하수슬러지가 수거되고, 수건된 유기물은 최초 호퍼(110)로 투입된다.In the present invention configured as described above, organic matters to be carbonized, that is, general household waste, contaminants, food waste, and sewage sludge are collected, and the toweled organic matter is introduced into the first hopper 110.

호퍼(110)를 통하여 믹서기(100) 내부로 투입된 유기물은 커터기(120)를 통하여 일정한 크기로 분쇄되고, 일정 크기로 분쇄된 유기물은 스크류(130)에 의해 믹싱되면서 배출구(140)로 이송된다.The organic material introduced into the mixer 100 through the hopper 110 is pulverized to a predetermined size through the cutter 120, and the organic material pulverized to a predetermined size is mixed with the screw 130 and then transferred to the outlet 140.

상기와 같이 배출구(140)를 통과한 유기물은 제1컨베이어(200)에 의해 이송됨과 동시에 본체(310) 한쪽에 형성된 투입구(330)를 통하여 회전가열통(350) 내부로 투입된다. 이때 회전가열통(350) 내부는 열공급통로(320)와 연결된 열풍발생장치로 부터 열이 공급되어 유기물이 열분해가 이루어질 수 있도록 적정한 100~250℃의 온도대가 형성된 상태이다.As described above, the organic material having passed through the outlet 140 is transported by the first conveyor 200 and is introduced into the rotary heating tube 350 through the inlet 330 formed at one side of the main body 310. At this time, the inside of the rotary heating tube 350 is a state in which a suitable temperature range of 100 ~ 250 ℃ is formed so that heat is supplied from the hot air generating device connected to the heat supply passage 320 so that organic matter can be pyrolyzed.

상기와 같은 상태에서 회전가열통(350) 내부로 열이 공급되면 상기한 회전가열통(350)은 구동부(340)에 의해 회전하면서 내부 자체 열로 유기물을 직접 가열시키고, 회전가열통(350) 내부에 장치되어 있는 로터리 스크류(360)는 유기물을 골고루 건조시킴과 동시에 건조된 유기물을 제2컨베이어(400)측으로 이송시킨다.When heat is supplied into the rotary heating tube 350 in the above state, the rotary heating tube 350 rotates by the driving unit 340 to directly heat the organic material with its own internal heat, and inside the rotary heating tube 350. Rotary screw 360 is installed in the evenly dried organic material and at the same time transfer the dried organic material to the second conveyor (400) side.

건조기(300)를 통과한 유기물이 제2컨베이어(400)에 의해 내부로 투입되면 탄화로(500)는 유기물을 600~900℃의 고온에서 간접 가열 건조시켜 유기물을 탄화시킨다.When the organic material passing through the dryer 300 is introduced into the inside by the second conveyor 400, the carbonization furnace 500 carbonizes the organic material by indirectly heating and drying the organic material at a high temperature of 600 to 900 ° C.

이를 더욱 상세하게 설명하면 제2컨베이어(400)에 의해 이송된 유기물이 투입구(570)를 통해 투입되면 케이싱(530) 내부에 형성된 회전스크류(540)에 의해 배출구(520)로 이송되는 과정을 거친다. 이때 회전스크류(540)를 따라 이송되는 과정에서 케이싱(530) 몸체를 밀실하게 차단하고 있던 간접가열통(550)은 열풍발생장치로 부터 발생된 열이 열유입구(560)를 통하여 내부로 유입되면 유기물이 열분해가 가능한 온도대로 상승하면서 유기물을 간접 가열 건조시키면서 탄화하고, 탄화하면서 발생된 가스는 가스배출구(570)를 통하여 외부로 배출된다.In more detail, when the organic material transferred by the second conveyor 400 is introduced through the inlet 570, the organic material is transferred to the outlet 520 by the rotating screw 540 formed in the casing 530. . At this time, the indirect heating barrel 550, which was tightly blocking the casing 530 body in the process of being transported along the rotating screw 540, when the heat generated from the hot air generator is introduced into the inside through the heat inlet 560. As the organic material rises to a temperature at which pyrolysis is possible, the organic material is carbonized while indirectly heating and drying, and the gas generated while carbonizing is discharged to the outside through the gas outlet 570.

이후, 탄화로(500)의 배출구(520)를 통해 건조된 유기물이 투입구(610)를 통하여 안정화로(600) 내부에 유입되면 케이싱(620) 내부에 형성된 회전스크류(630)에 의해 노즐(640)측으로 이송되고, 이송되는 과정에서 케이싱(620) 외부를 밀실하게 감싸 열을 내부로 공급케 하여 유기물을 안정화통(680)에서 완전 탄화처리 되며, 이때의 열은 열유입구(660)를 통해 열배출구(670)로 배출된다.Thereafter, when the organic material dried through the outlet 520 of the carbonization furnace 500 is introduced into the stabilization furnace 600 through the inlet 610, the nozzle 640 is formed by the rotating screw 630 formed in the casing 620. In the process of being transferred to the side, the casing 620 is tightly wrapped so that the heat is supplied to the inside so that the organic matter is completely carbonized in the stabilization container 680, and the heat is heated through the heat inlet 660. It is discharged to the outlet 670.

한편, 탄화된 탄화물은 노즐(640)을 통과하면서 외부로 배출되기 전에 급속냉각기(650)에 냉각되어 외부로 배출되는 것이며, 탄화물은 사용 목적에 따라 탈수보조제, 복토, 연료화, 토양개선제, 활성탄 제조원료로 재활용하면 되는 것이다.On the other hand, the carbonized carbide is cooled in the rapid cooler 650 before being discharged to the outside while passing through the nozzle 640 and discharged to the outside, the carbide is dehydration aid, cover, fuelization, soil improver, activated carbon production according to the purpose of use It can be recycled as raw materials.

이상에서 살펴본 바와 같이 본 발명에 의하면, 일반쓰레기, 협잡물, 음식물쓰레기, 하수슬러지등과 같은 유기물이 건조 탄화처리 되고, 탄화된 탄화물은 사용 목적에 따라 탈수보조제, 복토, 연료화, 토양개선제, 활성탄 제조원료로 재활용할 수 있는 등의 효과가 있는 것이다.As described above, according to the present invention, organic matters such as general garbage, contaminants, food waste, sewage sludge and the like are dried and carbonized, and the carbides are dehydrated aid, cover, fuelization, soil improver, activated carbon production according to the purpose of use. The effect is that it can be recycled as a raw material.

이상에서는 본 발명을 특정의 바람직한 실시예를 참고하여 설명하였으나, 본 발명은 상기한 실시예에 한정되지 아니하며 본 발명의 요지를 벗어나지 않는 범위에서 통상의 지식을 가진자에 의해 다양한 변경과 수정이 이루어질 수 있는 것임을밝혀둔다.The present invention has been described above with reference to specific preferred embodiments, but the present invention is not limited to the above embodiments and various changes and modifications may be made by those skilled in the art without departing from the gist of the present invention. Make sure you can.

Claims (4)

삭제delete 탄화하고자 하는 유기물이 투입되는 호퍼(110)와;A hopper 110 into which the organic material to be carbonized is introduced; 상기 호퍼(110) 하단에 위치하고 투입되는 유기물을 일정한 크기로 분쇄하는 커터기(120)가 내부 상단에 형성되며 이 커터기(120) 하단에는 일정 크기로 분쇄된 유기물이 낙하되면 유기물을 믹싱시키면서 배출구(140)로 이동시키는 스크류(130)가 구비되는 믹서기(100)와; 상기 스크류(130)의 배출구(140)를 통과한 유기물이 제1컨베이어(200)에 의해 내부로 투입되면 250℃의 고온으로 직접 가열 건조시키고 건조된 유기물은 제2컨베이어(400)측으로 이동시키는 건조기(300)와; 상기 건조기(300)를 통과한 유기물이 제2컨베이어(400)에 의해 내부로 투입되면 다시 유기물을 800℃의 고온에서 간접 가열 건조시켜 탄화시키는 탄화로(500))와; 상기 탄화로(500)를 통과한 유기물이 내부로 투입되면 이를 활성탄으로 제조되게 하는 안정화로(600)로 이루어진 연속식 유기물 탄화로 시스템에 있어서, 상기 건조기(300)는 일단에는 열풍발생장치로 부터 열이 공급되는 열공급통로(320)가 형성되고 타단에는 제1컨베이어(200)에 의해 이송된 유기물이 내부로 투입되게 하는 투입구(330)가 각각 형성되는 본체(310)와, 상기 열공급통로(320)와 투입구(330) 사이에 회전될 수 있도록 설치되고 내부로 열이 공급되면 구동부(340)에 의해 회전하면서 유기물을 직접 가열시키는 회전가열통(350)과, 상기 회전가열통(350) 내부에 위치하고 유기물이 골고루 건조되게 하면서 제2컨베이어(400)측으로 이송되게 하는 로터리 스크류(360)로 구성되는 것을 특징으로 하는 연속식 유기물 탄화로 시스템.The cutter 120 is disposed at the bottom of the hopper 110, and the organic material is crushed to a predetermined size is formed at the upper end, and when the organic material pulverized to a predetermined size falls at the bottom of the cutter 120, the outlet 140 while mixing the organic material. A mixer (100) having a screw (130) for moving to; When the organic material that has passed through the outlet 140 of the screw 130 is introduced into the interior by the first conveyor 200, the dryer is directly heated and dried at a high temperature of 250 ° C., and the dried organic material is moved to the second conveyor 400. 300; When the organic material passed through the dryer 300 is introduced into the inside by the second conveyor 400, the carbonization furnace 500 for carbonizing the organic material by indirect heat drying at a high temperature of 800 ℃ again; In the continuous organic carbonization system consisting of a stabilization furnace 600 to make the organic matter passed through the carbonization furnace 500 is made into activated carbon, the dryer 300 at one end from the hot air generator A heat supply passage 320 in which heat is supplied is formed, and at the other end, a main body 310 in which an injection hole 330 is formed to be introduced into the organic material transferred by the first conveyor 200, and the heat supply passage 320 is formed. ) Is installed so as to be rotated between the inlet 330 and the inside of the rotary heating tube 350, which is heated by the driving unit 340 to directly heat the organic material while being rotated by the driving unit 340. Continuous organic carbonization system characterized in that it consists of a rotary screw 360 is positioned and transported to the second conveyor 400 side while allowing the organics to be evenly dried. 제2항에 있어서, 상기 탄화로(500)는 일단 상부에는 제2컨베이어(400)에 의해 이송된 유기물이 내부로 투입되게 하는 투입구(510)가 형성되고 타단 저면에는 건조된 유기물이 아래 방향으로 배출되게 하는 배출구(520)가 일체로 형성되는 케이싱(530)과, 상기 케이싱(530) 내부에 장치되고 투입된 유기물을 일방향으로 이송시키는 회전스크류(540)와, 상기 케이싱(530) 몸체를 밀실하게 차단하며 열풍발생장치로 부터 발생된 열이 내부로 유입되면 간접 가열시킬 수 있도록 일단에는 열유입구(560)가 형성되고 타단에는 건조하면서 발생된 가스를 외부로 배출되게 하는 가스배출구(570)를 갖는 간접가열통(550)으로 구성되는 것을 특징으로 하는 연속식 유기물 탄화로 시스템.According to claim 2, wherein the carbonization furnace 500 has an inlet 510 is formed at the top to allow the organic material conveyed by the second conveyor 400 is introduced into the inside, and the dried organic material is downward on the other end. The casing 530 is formed integrally with the discharge port 520 to be discharged, the rotating screw 540 for conveying the organic material installed in the casing 530 in one direction, and the casing 530 body tightly A heat inlet 560 is formed at one end so as to be indirectly heated when heat generated from the hot wind generator is introduced into the inside, and a gas outlet 570 is formed at the other end to discharge the generated gas to the outside. Continuous organic carbonization system, characterized in that consisting of indirect heating tube (550). 제2항에 있어서, 상기 안정화로(600)는 탄화로(500)의 배출구(520)와 연결되는 투입구(610)가 상단에 형성되고 내부에 회전스크류(630)가 장치되는 케이싱(620)과, 상기 회전스크류(630)의 끝단에 연결 설치되어 회전스크류(630)를 따라 이송된 유기물을 급속냉각기(650)로 보내는 노즐(640)과, 상기 케이싱(620) 외부를 밀실하게 감싸 열을 내부로 공급케 하여 유기물이 완전 탄화될 수 있도록 한쪽에는 열유입구(660)가 형성되고 타단에서 열배출구(670)가 형성되는 안정화통(680)으로 구성되는 것을 특징으로 하는 연속식 유기물 탄화로 시스템.The casing 620 of claim 2, wherein the stabilization furnace 600 has an inlet 610 connected to the outlet 520 of the carbonization furnace 500 at an upper end thereof, and a rotating screw 630 is provided therein. The nozzle 640 is connected to the end of the rotating screw 630 to send the organic matter transported along the rotating screw 630 to the rapid cooler 650, and the casing 620 is tightly wrapped to enclose the inside of the heat. Continuous organic carbonization system, characterized in that consisting of a stabilization barrel 680 is formed in the heat inlet 660 is formed on one side and the heat outlet 670 is formed at the other end so that the organic matter is completely carbonized.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100992590B1 (en) * 2008-05-14 2010-11-05 황적조 Device for grinding and drying sluge and sluge dryer
KR101933111B1 (en) 2017-07-21 2019-03-15 주식회사 한기실업 Pyrolysis carbonizing machine

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100992590B1 (en) * 2008-05-14 2010-11-05 황적조 Device for grinding and drying sluge and sluge dryer
KR101933111B1 (en) 2017-07-21 2019-03-15 주식회사 한기실업 Pyrolysis carbonizing machine

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