KR20110004781U - A dry-distillationing and made oil equipment by recycling exhaust gas - Google Patents

A dry-distillationing and made oil equipment by recycling exhaust gas Download PDF

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KR20110004781U
KR20110004781U KR2020090014483U KR20090014483U KR20110004781U KR 20110004781 U KR20110004781 U KR 20110004781U KR 2020090014483 U KR2020090014483 U KR 2020090014483U KR 20090014483 U KR20090014483 U KR 20090014483U KR 20110004781 U KR20110004781 U KR 20110004781U
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warm
waste synthetic
exhaust gas
conveyor
dry
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KR2020090014483U
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KR200454813Y1 (en
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최현준
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최현준
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B23/00—Heating arrangements
    • F26B23/001—Heating arrangements using waste heat
    • F26B23/002—Heating arrangements using waste heat recovered from dryer exhaust gases
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/006—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects the gas supply or exhaust being effected through hollow spaces or cores in the materials or objects, e.g. tubes, pipes, bottles
    • 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
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/62—Plastics recycling; Rubber recycling

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

본 고안은 폐합성수지류를 건류 유화시키기 위해 건류탱크를 가열하는 동안 발생하는 배기가스를 재활용하여, 건류탱크에 투입되는 폐합성수지류를 건조시키는데 사용하는데 다시 사용하는 건류유화장치에 관한 고안이다.The present invention relates to a dry liquor emulsifying apparatus that is reused to dry waste synthetic resins fed to a dry distillation tank by recycling the exhaust gas generated while the dry distillation tank is heated to emulsify the waste synthetic resin.

본 고안은 폐합성수지류를 건류탱크로 이송하는 컨베이어에 있어서, 상기 컨베이어의 상측에는 컨베이어이송밸트의 상부에 폐합성수지이송공간부가 형성되도록 이격되어 온기덕트가 설치되고; 상기 컨베이어 상단부에는 상기 온기덕트와 연통되도록 건류탱크 가열부의 배기관이 연결되어 상기 건류탱크 가열부에서 배기되는 배기가스가 유입되도록 하며; 상기 온기덕트 하단부는 상기 컨베이어 폐합성수지이송공간부로 절곡되어 온기배출구가 형성됨으로써 상기 온기덕트의 온기가 폐합성수지이송공간부로 배출되도록 하는 것을 특징으로 한다.The present invention is a conveyor for transporting the waste synthetic resin to the dry distillation tank, the warm duct is installed on the upper side of the conveyor spaced apart so that the waste synthetic resin transfer space is formed on the conveyor transfer belt; An exhaust pipe of the distillation tank heating unit is connected to an upper end of the conveyor to communicate with the warm duct so that exhaust gas exhausted from the distillation tank heating unit is introduced; The lower end of the warm duct is bent to the conveyor waste synthetic resin transfer space portion is formed by the warm air outlet is characterized in that the warm air of the warm duct is discharged to the waste synthetic resin transfer space.

따라서, 본 고안은 건류탱크를 가열하면서 배출되는 배기가스를 재활용하여 폐합성수지류를 건조시키으로써 건류효율이 향상되며, 건류하고자 하는 폐합성수지류의 건조상태가 양호해 건류탱크를 가열하기 위한 전기의 소모가 줄어 매우 경제적이다.Therefore, the present invention improves dry efficiency by drying waste synthetic resins by recycling exhaust gas discharged while heating a dry tank, and the dry state of waste synthetic resins to be dried is satisfactory. It is very economical with less consumption.

Description

배기가스를 재활용하는 건류유화장치{A dry-distillationing and made oil equipment by recycling exhaust gas}A dry-distillationing and made oil equipment by recycling exhaust gas}

본 고안은 폐합성수지류를 건류 유화시키기 위해 건류탱크를 가열하는 동안 발생하는 배기가스를 재활용하여, 건류탱크에 투입되는 폐합성수지류를 건조시키는데 사용하는데 다시 사용하는 건류유화장치에 관한 고안이다.The present invention relates to a dry liquor emulsifying apparatus that is reused to dry waste synthetic resins fed to a dry distillation tank by recycling the exhaust gas generated while the dry distillation tank is heated to emulsify the waste synthetic resin.

건류유화장치는 자연분해가 되지 않는 폐합성수지를 고온으로 가열된 건류탱크에 넣어 융융시키면서 건류되는 동안 발생하는 건류가스를 포집하여 유화시킴으로써 액화연료를 얻고 있다.The distillation emulsion system obtains liquefied fuel by collecting and emulsifying the distillate gas generated during dry distillation while melting the synthetic resin which is not decomposed into a distillation tank heated to a high temperature.

이를 위해 건류탱크 하부에 구비된 가열부에 의해 건류탱크를 고온으로 가열한 후, 컨베이어에 의해 폐합성수지류를 건류탱크 상부의 투입구로 투입되고, 투입된 폐합성수지는 고온의 건류탱크 내부에서 용융되어 건류된다.To this end, after heating the distillation tank to a high temperature by a heating unit provided at the bottom of the distillation tank, the waste synthetic resin is introduced into the inlet of the top of the distillation tank by a conveyor, and the injected waste synthetic resin is melted in the hot distillation tank to dry do.

그러나, 건류탱크 내부로 투입되는 폐합성수지류가 습한 상태로 투입되기 때문에 용융이 되는데 오랜 시간이 소요되고, 가열부를 가열하기 위한 전기도 많이 소요되어 비경제적이다.However, since the waste synthetic resin introduced into the dry distillation tank is put in a humid state, it takes a long time to be melted, and a lot of electricity for heating the heating part is uneconomical.

본 고안은 상기와 같은 종래 문제점을 해결하고자 안출된 고안으로서, 건류를 위해 건류탱크로 투입되는 폐합성수지류가 건조된 상태로 투입되어 용용효율이 양호하고 가열을 위한 전기료를 줄일 수 있도록 함에 목적이 있다.The present invention is devised to solve the conventional problems as described above, the purpose of the waste synthetic resin to be put into the dry distillation tank for dry drying is put into a dry state, so that the melting efficiency is good and the electric charge for heating is reduced. have.

또한, 본 고안은 배기되어 버려지는 가열부의 배기가스를 재활용함에 목적이 있다.In addition, the present invention has an object to recycle the exhaust gas of the heating portion to be exhausted.

본 고안은 상기와 같은 목적을 위해 폐합성수지류를 건류탱크로 이송하는 컨베이어에 있어서, 상기 컨베이어의 상측에는 컨베이어이송밸트의 상부에 폐합성수지이송공간부가 형성되도록 이격되어 온기덕트가 설치되고; 상기 컨베이어 상단부에는 상기 온기덕트와 연통되도록 건류탱크 가열부의 배기관이 연결되어 상기 건류탱크 가열부에서 배기되는 배기가스가 유입되도록 하며; 상기 온기덕트 하단부는 상기 컨베이어 폐합성수지이송공간부로 절곡되어 온기배출구가 형성됨으로써 상기 온기덕트의 온기가 폐합성수지이송공간부로 배출되도록 하는 것을 특징으로 한다.The present invention is a conveyor for transporting the waste synthetic resin to the dry distillation tank for the above purpose, wherein the warm synthetic duct is installed on the upper side of the conveyor spaced apart so that the waste synthetic resin transfer space is formed; An exhaust pipe of the distillation tank heating unit is connected to an upper end of the conveyor to communicate with the warm duct so that exhaust gas exhausted from the distillation tank heating unit is introduced; The lower end of the warm duct is bent to the conveyor waste synthetic resin transfer space portion is formed by the warm air outlet is characterized in that the warm air of the warm duct is discharged to the waste synthetic resin transfer space.

본 고안은 건류탱크 가열부의 배기관 끝단부는 외부로 인출되어 배기가스가 외부로 배출되도록 하며, 상기 배기관의 끝단부에는 배기가스에 의해 가열되어 열기를 축적하는 온기축열부가 배기관을 감싸며 설치되고, 상기 온기축열부와 온기덕 트가 연통되어 상기 온기축열부에서 축열된 온기가 온기공급관을 통해 온기덕트로 공급되는 것을 특징으로 한다.According to the present invention, the exhaust pipe end of the drying tank heating unit is drawn to the outside so that the exhaust gas is discharged to the outside, and an end portion of the exhaust pipe is installed with a warm heat storage unit that is heated by the exhaust gas to accumulate heat and surrounds the exhaust pipe. The heat storage unit and the warm duct is in communication with each other, characterized in that the heat stored in the warm heat storage unit is supplied to the warm duct through the warm air supply pipe.

본 고안의 온기축열부는, 상기 배기관을 감싸며 형성되어 배기가스의 열에 의해 가열되는 온열저장부; 상기 온열저장부 내부에 구비되는 열축적관; 및, 상기 온열저장부의 끝단에 설치되는 송풍기로 이루어지는 것을 특징으로 한다.Warm storage unit of the present invention, the heat storage unit is formed surrounding the exhaust pipe is heated by the heat of the exhaust gas; A heat storage tube provided inside the heat storage unit; And a blower installed at an end of the heat storage unit.

본 고안의 온열저장부는 지그재그 형태로 절곡되어 온열의 축적율을 향상시키는 것을 특징으로 한다.The heat storage unit of the present invention is bent in a zigzag form to improve the accumulation rate of heat.

본 고안은 건류탱크를 가열하면서 배출되는 배기가스를 재활용하여 폐합성수지류를 건조시키으로써 건류효율이 향상된다.The present invention improves the drying efficiency by drying the waste synthetic resin by recycling the exhaust gas discharged while heating the drying tank.

또한, 본 고안은 건류하고자 하는 폐합성수지류의 건조상태가 양호해 건류탱크를 가열하기 위한 전기의 소모가 줄어 매우 경제적이다.In addition, the present invention is very economical to reduce the consumption of electricity for heating the dry distillation tank because the dry state of the waste synthetic resin to be dried is good.

또한, 본 고안은 배기가스의 열을 보다 효율적으로 축적할 수 있는 매우 유용한 고안이다.In addition, the present invention is a very useful design that can more efficiently store the heat of the exhaust gas.

이하, 본 고안의 가장 바람직한 일 실시예의 구성을 첨부한 도면을 참고하여 설명하면 다음과 같다.Hereinafter, the configuration of the most preferred embodiment of the present invention with reference to the accompanying drawings as follows.

도 1은 본 발명의 일 실시예에 따른 건류유화장치의 예시도이다.1 is an illustration of a dry distillation apparatus according to an embodiment of the present invention.

도 1을 참조하면, 본 발명의 건류탱크(100)는 폐합성수지류를 투입하기 위한 투입구(110)가 상부에 구비되고, 하부에는 건류탱크(100)를 가열하기 위한 가열부(200)가 설치되며, 가열부(200)의 끝단에는 배기관(210)이 연결된다. 배기관(210)은 가열부(200)의 배기가스가 외부로 배출되도록 외부와 연통되어 설치된다.Referring to FIG. 1, the dry distillation tank 100 of the present invention has an inlet 110 for injecting waste synthetic resin thereon, and a heating unit 200 for heating the dry distillation tank 100 is installed at a lower portion thereof. The exhaust pipe 210 is connected to the end of the heating part 200. The exhaust pipe 210 is installed in communication with the outside so that the exhaust gas of the heating unit 200 is discharged to the outside.

배기관(210)의 끝단 상부에는 온기축열부(300)가 설치되는 것이 바람직하다. 온기축열부(300)는 소정의 공간부로 이루어져 온기축열부(300) 내부의 공기를 데워준다. Warm end heat storage unit 300 is preferably installed on the upper end of the exhaust pipe (210). The warm heat storage unit 300 is formed of a predetermined space to warm the air inside the warm heat storage unit 300.

도 2는 본 발명의 일 실시예에 따른 건류유화장치의 온기축열부를 도시한 일부 사시도 및 단면도이다.2 is a partial perspective view and a cross-sectional view showing the warm heat storage unit of the dry distillation emulsion according to an embodiment of the present invention.

온기축열부(300)는 온기저장부(310)와 송풍기(320) 및 열축적관(330), 온기공급관(340)으로 이루어진다.The warm heat storage unit 300 includes a warm storage unit 310, a blower 320, a heat storage pipe 330, and a warm air supply pipe 340.

온기저장부(310)는 지그재그 형태로 절곡 형성되어 온열 축열효율을 향상시키며, 온기저장부(310) 내부에는 다수개의 열축적관(330)이 구비되어 열을 축적하도록 하는 것이 바람직하다. 온기저장부(310)의 끝단에는 송풍기(320)가 설치된다. 온기공급관(340)의 일측 끝단은 온기저장부(310)의 선단에 연결되고 타측 끝단은 컨베이어(400)로 연결된다.The warmth storage unit 310 is bent in a zigzag form to improve the thermal heat storage efficiency, and a plurality of heat storage tubes 330 are provided inside the warmth storage unit 310 to accumulate heat. The blower 320 is installed at the end of the warmth storage unit 310. One end of the warm air supply pipe 340 is connected to the front end of the warm storage unit 310 and the other end is connected to the conveyor 400.

도 3은 본 발명의 일 실시예에 따른 건류유화장치의 컨베이어 측 일부 단면도이다.3 is a partial cross-sectional view of the conveyor side of a dry distillation apparatus according to an embodiment of the present invention.

도 3에 도시된 바와 같이, 컨베이어(400)는 폐합성수지류를 건류탱크(100) 측으로 이송하기 위한 이송벨트(410)가 롤러(420)에 권선되어 있다. 컨베이어(400) 이송벨트(410) 상부에는 폐합성수지이송공간(430)이 형성되고, 폐합성수지이송공간(430)의 상측으로 이격되어 온기덕트(440)가 소정의 공간으로 형성된다.As shown in FIG. 3, the conveyor 400 has a conveying belt 410 wound around the roller 420 to convey waste synthetic resin to the dry distillation tank 100. The waste synthetic resin transfer space 430 is formed on the conveyor belt 410, and the warm duct 440 is spaced above the waste synthetic resin transfer space 430 to form a predetermined space.

온기덕트(440)의 선단은 하측으로 절곡되어 온기덕트(440)를 통해 이송하는 온기가 폐합성수지이송공간(430)으로 배출되도록 온기배출구(450)가 형성된다.The tip of the warm duct 440 is bent downward to form a warm outlet 450 so that the warm air conveyed through the warm duct 440 is discharged to the waste synthetic resin transport space 430.

상기와 같이 구성되는 본 발명의 일 실시예에 따른 건류유화장치의 작동을 설명하면 다음과 같다.Referring to the operation of the dry distillation apparatus according to an embodiment of the present invention configured as described above are as follows.

건류탱크(100) 하부의 가열기(200)에 의해 고온으로 가열된 상태에서 컨베이 어(400)를 작동시킨 후 롤러(420)와 함께 회전하는 이송벨트(410)의 상부에 폐합성수지를 올린다.After operating the conveyor 400 in a state heated to a high temperature by the heater 200 under the distillation tank 100, the waste synthetic resin is placed on the upper portion of the conveyance belt 410 rotating with the roller 420.

폐합성수지는 이송벨트(410)를 타고 건류탱크(100)의 투입구(110)를 통해 건류탱크(100) 내부로 투입되며, 고온으로 가열된 건류탱크(100) 내부에서 용융되면서 건류 유화된다.The waste synthetic resin is introduced into the dry distillation tank 100 through the inlet 110 of the dry distillation tank 100 by the transfer belt 410, and is dried and emulsified in the dry distillation tank 100 heated to a high temperature.

이때, 건류탱크(100)를 가열하는 가열부(200)에서는 가열을 하면서 발생하는 고온의 배기가스가 배기관(210)을 통해 외부로 배출된다.At this time, the heating unit 200 for heating the dry distillation tank 100 is discharged to the outside through the exhaust pipe 210 of the high temperature generated while heating.

배기관(210)을 통해 배출되는 배기가스는 배기관(210) 끝단부 상부에 설치된 온기축열부(300)에 열을 저장하고 이는 다시 온기공급관(340)을 통해 컨베이어(400) 측으로 공급된다.The exhaust gas discharged through the exhaust pipe 210 stores heat in the warm heat storage unit 300 installed at the upper end of the exhaust pipe 210, which is supplied to the conveyor 400 through the warm air supply pipe 340.

이를 보다 구체적으로 설명하면, 배기관(210)을 통해 배기가스가 배출되는 동안 배기관(210) 상부에 설치된 온기축열부(300)의 온기저장부(310) 내부의 공기가 데워진다. 데워지는 공기는 열축적관(330)에 축적이 되어 축적율을 향상시킨다.In more detail, the air inside the warm storage unit 310 of the warm heat storage unit 300 installed on the exhaust pipe 210 is heated while the exhaust gas is discharged through the exhaust pipe 210. The warmed air is accumulated in the heat storage pipe 330 to improve the accumulation rate.

데워진 온기는 송풍기(320)의 송풍에 의해 온기공급관(340)을 통해 컨베이어(400) 상부의 온기덕트(440)로 공급되며, 온기가 온기덕트(440)를 지나는동안 컨 베이어(400)의 폐합성수지이송공간(430)의 공기를 데워 이송벨트(410)를 타고 이송되는 폐합성수지를 건조시킨다.The warmed warm air is supplied to the warm duct 440 on the conveyor 400 through the warm air supply pipe 340 by the blowing air of the blower 320, and the waste of the conveyor 400 while the warm air passes through the warm duct 440. The air in the synthetic resin transport space 430 is dried to dry the waste synthetic resin which is transported on the transport belt 410.

온기덕트(440)를 통과한 온기는 하부로 절곡된 온기덕트(440)에 의해 폐합성수지이송공간(430)으로 형성된 온기배출구(450)를 통해 배출된다. 따라서, 이송벨트(410)을 타고 폐합성수지이송공간(430)으로 이송하는 폐합성수지는 재차 건조가 이루어지게 된다.The warmth that has passed through the warmth duct 440 is discharged through the warmth outlet 450 formed by the waste resin transfer space 430 by the warmer duct 440 bent downward. Therefore, the waste synthetic resin to be transported to the waste synthetic resin transfer space 430 by the transfer belt 410 is dried again.

따라서, 건류탱크(100)로 투입되는 폐합성수지류의 건조가 확실하게 이루어져 용융효율이 향상되고, 폐합성수지류의 용융을 위해 가열부(200)를 가열하는 전기의 사용을 줄일 수 있게 된다.Therefore, the drying of the waste synthetic resin introduced into the dry distillation tank 100 is ensured, thereby improving the melting efficiency and reducing the use of electricity for heating the heating unit 200 for melting the waste synthetic resin.

도 1은 본 발명의 일 실시예에 따른 건류유화장치의 예시도1 is an illustration of a dry distillation apparatus according to an embodiment of the present invention

도 2는 본 발명의 일 실시예에 따른 건류유화장치의 온기축열부를 도시한 일부 사시도 및 단면도2 is a partial perspective view and a cross-sectional view showing the warm heat storage unit of the dry distillation apparatus according to an embodiment of the present invention

도 3은 본 발명의 일 실시예에 따른 건류유화장치의 컨베이어 측 일부 단면도Figure 3 is a partial cross-sectional view of the conveyor side of the dry distillation apparatus according to an embodiment of the present invention

<도면의 주요부분에 대한 부호설명><Code Description of Main Parts of Drawing>

100 : 건류탱크 110 : 투입구100: distillation tank 110: inlet

200 : 가열부 210 : 배기관200: heating section 210: exhaust pipe

300 : 온기축열부 310 : 온기저장부300: warm heat storage unit 310: warm storage unit

320 : 송풍기 330 : 열축적관320: blower 330: heat storage pipe

340 : 온기공급관 400 : 컨베이어340: hot water supply pipe 400: conveyor

440 : 온기덕트 450 : 온기배출구440: warmth duct 450: warmth outlet

Claims (4)

폐합성수지류를 건류탱크로 이송하는 컨베이어에 있어서,In the conveyor for transporting waste synthetic resins to the dry distillation tank, 상기 컨베이어의 상측에는 컨베이어이송밸트의 상부에 폐합성수지이송공간부가 형성되도록 이격되어 온기덕트가 설치되고;On the upper side of the conveyor is spaced apart so that the waste synthetic resin transfer space is formed on the upper portion of the conveyor transfer belt is installed warm ducts; 상기 컨베이어 상단부에는 상기 온기덕트와 연통되도록 건류탱크 가열부의 배기관이 연결되어 상기 건류탱크 가열부에서 배기되는 배기가스가 유입되도록 하며;An exhaust pipe of the distillation tank heating unit is connected to an upper end of the conveyor to communicate with the warm duct so that exhaust gas exhausted from the distillation tank heating unit is introduced; 상기 온기덕트 하단부는 상기 컨베이어의 폐합성수지이송공간부로 절곡되어 온기배출구가 형성됨으로써 상기 온기덕트의 온기가 폐합성수지이송공간부로 배출되도록 하는 것을 특징으로 하는 배기가스를 재활용하는 건류유화장치.The lower end of the warm duct is bent into the waste synthetic resin transfer space of the conveyor is formed warm water outlet so that the warmth of the warm duct is discharged to the waste synthetic resin transfer space, dry distillation oil recycling apparatus characterized in that. 제 1항에 있어서,The method of claim 1, 상기 건류탱크 가열부의 배기관 끝단부는 외부로 인출되어 배기가스가 외부로 배출되도록 하며,The exhaust pipe end of the drying tank heating unit is drawn to the outside to exhaust the exhaust gas to the outside, 상기 배기관의 끝단부에는 배기가스에 의해 가열되어 열기를 축적하는 온기축열부가 배기관을 감싸며 설치되고,At the end of the exhaust pipe is provided with a warm heat storage portion surrounding the exhaust pipe is heated by the exhaust gas to accumulate heat, 상기 온기축열부와 온기덕트가 연통되어 상기 온기축열부에서 축열된 온기가 온기공급관을 통해 온기덕트로 공급되는 것을 특징으로 하는 배기가스를 재활용하 는 건류유화장치.The warm heat emulsifying device for recycling the exhaust gas, characterized in that the warm heat storage unit and the warm duct is in communication with the warm heat stored in the warm heat storage unit is supplied to the warm duct through a warm air supply pipe. 제 2항에 있어서, 상기 온기축열부는,The warmth heat storage unit according to claim 2, 상기 배기관을 감싸며 형성되어 배기가스의 열에 의해 가열되는 온열저장부;A thermal storage part formed surrounding the exhaust pipe and heated by heat of exhaust gas; 상기 온열저장부 내부에 구비되는 열축적관; 및,A heat storage tube provided inside the heat storage unit; And, 상기 온열저장부의 끝단에 설치되는 송풍기로 이루어지는 것을 특징으로 하는 배기가스를 재활용하는 건류유화장치.Dry distillation apparatus for recycling the exhaust gas, characterized in that made of a blower installed at the end of the heat storage. 제 3항에 있어서,The method of claim 3, wherein 상기 온열저장부는 지그재그 형태로 절곡되어 온열의 축적율을 향상시키는 것을 특징으로 하는 배기가스를 재활용하는 건류유화장치.The thermal storage unit is a zig-zag bent in a zigzag form, dry distillation apparatus for recycling exhaust gas, characterized in that to improve the accumulation rate of heat.
KR20090014483U 2009-11-07 2009-11-07 Dry distillation unit to recycle exhaust gas KR200454813Y1 (en)

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