KR100612521B1 - Recycle system for worthless or useless material - Google Patents

Recycle system for worthless or useless material Download PDF

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KR100612521B1
KR100612521B1 KR1020027017047A KR20027017047A KR100612521B1 KR 100612521 B1 KR100612521 B1 KR 100612521B1 KR 1020027017047 A KR1020027017047 A KR 1020027017047A KR 20027017047 A KR20027017047 A KR 20027017047A KR 100612521 B1 KR100612521 B1 KR 100612521B1
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materials
component
unnecessary
components
vaporized
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KR20030011899A (en
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시바타아키라
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리스웃도 가부시키가이샤
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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B1/00—Retorts
    • C10B1/10—Rotary retorts
    • 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
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/10—Biofuels, e.g. bio-diesel
    • 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
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)
  • Coke Industry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

종래보다도 저비용으로 할 수 있는 불필요한 자재의 재생 시스템으로서, 불필요한 자재를 열분해하여 탄화성분을 얻고, 또한 불필요한 자재로부터의 기화성분을 냉각액화하고, 냉각액화한 성분을 분류하여 유용물질을 뽑아내도록 한 것을 특징으로 한다.It is a regeneration system of unnecessary materials which can be made at a lower cost than before, and thermally decomposes unnecessary materials to obtain a carbonized component, cools the vaporized components from unnecessary materials, classifies the cooled liquid components, and extracts useful materials. It features.

Description

불필요한 자재의 재생 시스템{RECYCLE SYSTEM FOR WORTHLESS OR USELESS MATERIAL}Unnecessary material recycling system {RECYCLE SYSTEM FOR WORTHLESS OR USELESS MATERIAL}

본 발명은 불필요한 자재의 재생 시스템에 관한 것이다.The present invention relates to a recycling system of unnecessary materials.

건축용 자재의 생산시에 나오는 초승달 형상의 단재(端材)나, 댐 등에 쌓이는 유목·간벌재 등과 같은 천연목재(불필요한 자재)가 있다. 이 천연목재인 불필요한 자재로부터의 탄화(열분해)에 의한 목탄 등의 생산은 경제성의 문제에서 거의 실행되고 있지 않고, 제지용 칩으로 만들거나 소각이 이와 같은 천연목재의 주된 처리방법이다.There are natural timbers (unnecessary materials), such as crescent shaped cuts in the production of building materials, and driftwood and thinning timbers accumulated in dams. The production of charcoal and the like by carbonization (pyrolysis) from unnecessary materials, which are natural wood, is hardly carried out due to economic problems, and it is made from paper chips or incineration is the main treatment method of such natural wood.

또, 접착제나 도료와 같은 비천연물질이 부착된 건축폐재(불필요한 자재)가 있다. 이 건축폐재인 불필요한 자재로부터의 탄화(열분해)에 의한 목탄 등의 생산은 경제성이나 비천연물질로부터의 기화성분의 위험성의 문제에서 거의 실행되고 있지 않다.There are also construction wastes (unnecessary materials) to which non-natural substances such as adhesives and paints are attached. The production of charcoal and the like by carbonization (pyrolysis) from unnecessary materials, which are construction wastes, is hardly carried out in view of economics and the risk of vaporizing components from non-natural materials.

그래서 본 발명은 종래보다도 저렴한 비용으로 할 수 있는 불필요한 자재의 재생 시스템을 제공하려고 하는 것이다.Accordingly, the present invention is to provide a system for regenerating unnecessary materials which can be made at a lower cost than before.

상기 과제를 해결하기 위해 본 발명의 불필요한 자재의 재생 시스템은 불필 요한 자재를 열분해하여 탄화성분을 얻고, 또한 불필요한 자재로부터의 기화성분을 냉각액화하고 냉각액화한 성분을 분류(分溜)하여 유용물질을 뽑아내도록 한 것을 특징으로 한다.In order to solve the above problems, the unnecessary material recycling system of the present invention pyrolyzes unnecessary materials to obtain carbonized components, and further cools and vaporizes vaporized components from unnecessary materials and classifies the cooled liquids into useful materials. It is characterized in that the pull out.

이 재생 시스템에 의하면, 불필요한 자재를 열분해하여 얻게 된 탄화성분과 함께, 냉각액화한 성분을 분류하여 뽑아낸 물질도 유용물질로서 재이용할 수 있다. 즉, 종래는 처리에 곤란했던 기화성분의 유효이용을 꾀할 수 있다.According to this regeneration system, the material obtained by classifying and extracting the cooled liquid component as well as the carbonized component obtained by thermal decomposition of unnecessary materials can be reused as a useful substance. That is, the effective use of the vaporization component which was conventionally difficult to process can be aimed at.

또, 불필요한 자재의 열분해시의 기화성분을 냉각액화하여 기화성분을 소각처리하기 위한 배연의 제 2 차 배연 소각장치를 설치할 필요없이, 탄화시스템 설비의 저비용화를 꾀할 수 있다.In addition, it is possible to reduce the cost of the carbonization system equipment without the need to install a second flue gas incinerator for cooling the vaporized components during thermal decomposition of unnecessary materials to incinerate the vaporized components.

불필요한 자재는 예를 들면 건류(乾溜)에 의해 탄화시킬 수 있다.Unnecessary materials can be carbonized by dry distillation, for example.

분류로서는 온도분류나 화학분류를 예시할 수 있고, 정류탑 또는 감압·상압·가압온도분류, 초임계(超臨界)를 사용한 분류, 화학물질을 이용한 분류 또는 이들 조합으로 할 수 있다. 액화성분을 분류하는 온도는 그 유용성과 경제효율을 감안하여 설정하면 좋다.As classification, temperature classification and chemical classification can be illustrated, and it can be a rectification tower or pressure reduction, atmospheric pressure, pressurization temperature classification, classification using supercritical, classification using a chemical substance, or a combination thereof. The temperature for classifying the liquefied component may be set in consideration of its usefulness and economic efficiency.

불필요한 자재로서 건축용 자재의 생산시에 나오는 초승달 모양의 단재나, 댐 등에 쌓이는 유목·간벌재 등의 천연 목질성분을 예시할 수 있다. 목질계의 불필요한 자재로부터 얻을 수 있는 탄화물은 목탄으로서 이용할 수 있고, 또한 기화성분을 냉각액화하여 얻을 수 있는 목초액이나 목타르 오일 등을 분류하여 유용물질로서 정제하여 이용할 수 있다. 또, 냉각액화하는 온도는 예를 들면 약 -20℃에서 90℃ 정도로 설정할 수 있다.As an unnecessary material, natural wood components, such as a crescent-shaped cutting material which appears at the time of production of a building material, a driftwood and a thinning timber piled up in a dam etc. can be illustrated. Carbide obtained from the wood-based unnecessary material can be used as charcoal, and can be purified by use as a useful material by classifying wood vinegar, tar tar oil, etc. which can be obtained by cooling the vaporization component. In addition, the temperature to cool liquid can be set to about -20 degreeC to about 90 degreeC, for example.

또 불필요한 자재로서 목질성분에 접착제나 도료 등의 비천연물질이 부착된 건축폐재를 예시할 수 있다. 건축폐재의 탄화물질은 목탄으로서 이용할 수 있고, 또한 그 기화성분을 분류하여 목초액이나 목타르 오일과 같은 본래적으로 유용한 물질을 뽑아낼 수 있다. 이 때, 기화성분에서는 불순물질이나 위험물질도 분류되지만, 이들 불순물질이나 위험물질은 그 순수물질로서 정제하여 이용할 수도 있다. 또 냉각액화하는 온도는 예를 들면 약 -20℃에서 90℃ 정도로 설정할 수 있다.Moreover, as an unnecessary material, the building waste material to which wooden components adhered to non-natural substances, such as an adhesive and a paint, can be illustrated. The carbonized material of the building waste can be used as charcoal, and the vaporized components can be classified to extract inherently useful substances such as wood vinegar and tartar oil. At this time, impurities and dangerous substances are also classified as vaporized components, but these impurities and dangerous substances may be purified and used as the pure substance. In addition, the temperature to cool liquid can be set to about -20 degreeC to about 90 degreeC, for example.

또 불필요한 자재로서 합성수지재(플라스틱 폐재 등) 등을 예시할 수 있고, 마찬가지로 탄화성분 이외의 유용한 물질을 얻을 수 있다.Moreover, synthetic resin materials (plastic waste materials, etc.) etc. can be illustrated as an unnecessary material, and useful substances other than a carbonization component can be obtained similarly.

액화할 때의 간이한 냉각방법으로서 액화성분 자체에 의한 샤워링이나 간이형 장애판 등을 제안할 수 있다.As a simple cooling method at the time of liquefaction, the showering by a liquefaction component itself, a simple obstacle board, etc. can be proposed.

또, 액화곤란한 기화성분을 환류하여 탄화성분을 열분해하기 위한 열원으로서 이용해도 좋다. 이와 같이 구성하면 액화곤란한 기화성분을 목질성분의 열분해를 위한 연료로 할 수 있고, 또한 고온소성에 의해 액화곤란한 기화성분의 안전성을 보다 보장할 수 있다.Moreover, you may use as a heat source for refluxing the gasification component which is difficult to liquefy, and pyrolyzing a carbonization component. In this way, the liquefied difficult vaporized component can be used as a fuel for thermal decomposition of wood components, and the safety of the vaporized difficult liquefied component can be more ensured by high temperature firing.

상기한 재생 시스템에 의해 탄화성분을 얻을 수 있고, 또 유용물질을 뽑아낼 수 있다.By the above-mentioned regeneration system, a carbonized component can be obtained and useful materials can be taken out.

도 1은 본 발명의 불필요한 자재의 재생 시스템의 실시형태 1을 설명하기 위한 시스템도, 및1 is a system diagram for explaining Embodiment 1 of a waste material recycling system of the present invention, and

도 2는 본 발명의 불필요한 자재의 재생 시스템의 실시형태 2를 설명하기 위 한 시스템도이다.FIG. 2 is a system diagram for explaining Embodiment 2 of an unnecessary material recycling system of the present invention. FIG.

본 발명의 실시형태 1의 재생 시스템에 있어서는 불필요한 자재로서 건축용 자재의 생산시에 나오는 초승달 모양의 단재와, 댐 등에 쌓이는 유목·간벌재 등의 천연 목질성분을 이용했다.In the regeneration system of Embodiment 1 of this invention, natural wood components, such as a crescent-shaped cutting material which appears at the time of production of a building material, and the driftwood and thinning timber piled up in a dam etc. were used as unnecessary material.

상기 실시형태 1의 재생 시스템이 도 1에 나타나 있다. 이 시스템에 있어서 불필요한 자재는 불필요한 자재 거치장소(11)로부터 컨베이어(12), 파쇄기(13), 컨베이어(14), 건조기(15), 저장고(16)를 통해 탄화로(1)에 투입된다. 이 실시형태에 있어서는 로터리킬른(rotary kiln) 탄화로(1)가 사용되고 있다. '17'은 시동용 버너이다. 탄화성분은 탄화로(1)에서 탄저장고(18)로 회수되는데, 금속물질은 자선기(磁選機)(19)에 의해 분별되어 금속 저장고(20)로 회수된다.The reproduction system of the first embodiment is shown in FIG. In this system, unnecessary materials are fed into the carbonization furnace 1 through the conveyor 12, the crusher 13, the conveyor 14, the dryer 15, and the storage 16 from the unnecessary material storage place 11. In this embodiment, the rotary kiln carbonization furnace 1 is used. '17' is the starter burner. The carbonized component is recovered from the carbonization furnace 1 to the carbon storage 18, and the metal material is separated by the charity 19 and recovered into the metal storage 20.

기화성분은 수냉 컨덴서(2)로 회수된다. 수냉 컨덴서(2)에는 쿨링 타워(21), 냉각수 펌프(22)가 연결되어 있다. '23'은 가스 에어 히터, '24'는 건조팬이다. 액화냉각된 성분은 사이클론(25), 가스 시일 탱크(26), 액화성분 탱크(27), 송액 펌프(28)를 통해 증류가마(3)로 이송되어 정류탑(4), 분류받이 탱크(5)로 회수된다.The vaporized component is recovered by the water-cooled capacitor (2). The cooling tower 21 and the cooling water pump 22 are connected to the water cooling capacitor 2. '23' is the gas air heater and '24' is the drying fan. The liquefied cooled component is transferred to the distillation kiln (3) through the cyclone (25), gas seal tank (26), liquefaction component tank (27), and liquid feed pump (28) to the rectification tower (4) and the sorting tank (5). ) Is recovered.

이 시스템에 의해 목질계의 불필요한 자재를 로터리킬른 탄화로(1)에서 건류에 의해 열분해하여 탄화성분을 얻고, 불필요한 자재로부터의 기화성분을 수냉 컨덴서(2)에서 액화냉각온도를 약 -20℃에서 90℃ 정도로 설정하여 냉각액화하고, 냉각액화한 성분을 증류가마(3)에서 정류탑(4)으로 온도분류하여 분류받이 탱크(5)에 유용물질을 뽑아냈다.This system thermally decomposes woody materials by dry distillation in a rotary kiln carbonization furnace (1) to obtain carbonized components, and vaporizes the components from unnecessary materials at a liquid cooling condenser (2) at about -20 ° C. Cooling liquid was set at about 90 ° C., and the cooled liquid was temperature-divided from the distillation kiln 3 to the rectifying column 4 to extract useful materials from the sorting tank 5.

목질계의 불필요한 자재로부터 얻게 된 탄화물은 목탄으로 할 수 있다. 또, 불필요한 자재로부터의 기화성분의 냉각액화에 의해 얻게 된 목초액이나 목타르 오일 등을 분류하여 유용물질로서 정제할 수 있었다. 즉, 이 불필요한 자재의 재생 시스템에 의해 탄화성분을 얻고, 또한 유용물질을 뽑아낼 수 있었다.Carbide obtained from wood waste material can be charcoal. In addition, wood vinegar, moth tar oil and the like obtained by cooling liquefaction of vaporized components from unnecessary materials were classified and purified as useful substances. That is, the carbonization component was obtained by this reclaiming system of unnecessary materials, and useful materials were able to be taken out.

이 재생 시스템에 의하면, 불필요한 자재를 열분해하여 얻게 된 탄화성분과 함께, 기화성분을 냉각액화, 분류하여 뽑아낸 물질도 유용물질로서 재이용할 수 있어 종래보다도 전체적으로 저비용의 재생을 할 수 있는 이점이 있다.According to this regeneration system, in addition to the carbonized component obtained by pyrolyzing unnecessary materials, the material extracted by cooling and liquefying vaporized components can be reused as a useful material, which has the advantage of lower overall regeneration than before. .

종래는 천연목재나 건축폐재로부터 목탄생산을 실행하는 경우에는 공해방지를 위해 기화성분을 소각처리하기 위해 건류로 등의 목탄가마에는 2차 배연소각장치를 설치할 필요가 있어 비싸게 되어 버리는 문제가 있었다. 그러나, 본 발명의 실시형태는 불필요한 자재의 열분해시의 기화성분을 냉각액화하고 있고, 기화성분을 소각처리하기 위한 배연의 제 2차 배연소각장치를 설치할 필요는 없다. 즉, 탄화시스템 설비의 저비용화를 꾀하고, 종래는 처리가 곤란했던 기화성분의 유효이용을 꾀할 수 있는 이점도 있다.Conventionally, when charcoal production is performed from natural wood or construction waste, there is a problem in that it is necessary to install a secondary flue gas incinerator in a charcoal kiln such as a dry distillation furnace in order to incinerate vaporized components to prevent pollution. However, in the embodiment of the present invention, the vaporized component during the thermal decomposition of unnecessary materials is liquefied and it is not necessary to provide a secondary flue gas incinerator for incineration of the vaporized component. That is, there is also an advantage that the carbonization system equipment can be reduced in cost, and the effective use of the vaporized component, which has been difficult in the past, can be achieved.

또, 액화곤란한 기화성분을 유인팬(6) 등의 수단을 이용하여 탄화로(1)에 환류하고, 이 기화성분을 탄화성분을 제조할 때의 목질성분의 열분해를 위한 외부 공급연료로서 이용하고 있다. 이 액화곤란한 기화성분을 고온으로 소성하는 것에 의해 이 기화성분의 안전성을 보다 보장할 수 있는 이점이 있다.In addition, refluxing the liquefied vaporized component into the carbonization furnace 1 by means of an induction fan 6 or the like, and using this vaporized component as an external feed fuel for thermal decomposition of wood components when producing the carbonized component. have. There is an advantage that the safety of the vaporized component can be more assured by firing this liquefied vaporized component at a high temperature.

다음에 본 발명의 실시형태 2에 대해 실시형태 1과의 상위점을 중심으로 설 명한다.Next, the second embodiment of the present invention will be described focusing on differences from the first embodiment.

불필요한 자재로서는 목질성분에 접착제나 도료 등의 비천연물질이 부착된 건축폐재를 이용했다. 이 건축폐재로부터는 목탄 및 목초액이나 목타르 오일과 같은 물질을 뽑아내고 불순물질이나 위험물질을 제거했다.As an unnecessary material, the building waste material in which wooden components adhered to non-natural substances, such as an adhesive and a paint, was used. From these wastes, charcoal, woody liquor, and tartar oil were extracted, and impurities and dangerous substances were removed.

실시형태 2는 도 2에 도시되어 있다. 실시형태 1과 같이, 건축폐재를 로터리킬른 탄화로(1)에 운송하고, 탄화로(1)에서 건류에 의해 열분해하여 탄화성분을 얻는다. 한편, 건축폐재로부터의 기화성분은 실시형태 1과 달리, 세정식 컨덴서(2)에서 냉각액화온도를 약 -20℃에서 90℃ 정도로 설정하고, 샤워링하여 냉각액화한다. 이 세정식 컨덴서(2)에는 공냉식 냉각장치(31)가 연결되어 있다. 냉각액화한 성분을 증류가마(3)에서 정류탑(4)으로 온도분류하고, 목초액이나 목타르 오일 등의 본래적으로 유용한 물질 및 불순물질이나 위험물질을 각 분류받이 탱크(5)에 각각 뽑아냈다. 불순물질이나 위험물질은 그 순수물질로서 정제하여 이용할 수 있다.Embodiment 2 is shown in FIG. As in the first embodiment, the building waste material is transported to the rotary kiln carbonization furnace 1, and thermally decomposed by dry distillation in the carbonization furnace 1 to obtain a carbonized component. On the other hand, unlike the first embodiment, the vaporized component from the construction waste is set to about -20 ° C to about 90 ° C by the cooling type condenser 2, and is showered to cool the liquid. An air-cooled cooling device 31 is connected to this washing capacitor 2. The cooled liquefied components were temperature-divided from the distillation kiln (3) to the rectification tower (4), and originally useful substances such as wood vinegar and tar tar oil, and impurities or dangerous substances were extracted to each sorting tank (5). . Impurities or dangerous substances can be purified and used as the pure substance.

또 다른 간이한 냉각방법으로서 간이형 장애판 등을 들 수 있다.Another simple cooling method may be a simple barrier plate.

또, 불필요한 자재로서는 이상의 것 이외에도 합성수지재(플라스틱 폐재 등) 등을 예시할 수 있고, 마찬가지로 탄화성분이나 유용물질을 얻을 수 있다. 또, 불필요한 자재의 종류에 관계없이 실시형태 1 또는 2 그 이외의 동등한 시스템을 사용할 수 있다.In addition, as an unnecessary material, a synthetic resin material (plastic waste material etc.) etc. can be illustrated besides the above, and a carbonization component and a useful substance can be obtained similarly. In addition, irrespective of the kind of unnecessary material, equivalent systems other than Embodiment 1 or 2 can be used.

본 발명은 상기한 바와 같은 구성이고, 천연목재, 건축폐재, 플라스틱 폐재 등의 불필요한 자재로부터 탄화성분을 저비용으로 얻을 수 있고, 목탄 등으로서 재이용할 수 있다. 또, 불필요한 자재로부터의 기화성분을 냉각액화 및 분류하여 탄화성분 이외의 유용물질을 뽑아내어 재이용할 수 있다. 위험물질 등도 순수물질로 정제하여 재이용할 수 있다. 따라서, 불필요한 자재의 재생 시스템으로서 바람직하다.The present invention has the configuration as described above, and carbonized components can be obtained at low cost from unnecessary materials such as natural wood, construction waste, and plastic waste, and can be reused as charcoal or the like. In addition, by evaporating and classifying vaporized components from unnecessary materials, useful materials other than the carbonized components can be extracted and reused. Dangerous substances can also be purified and reused as pure substances. Therefore, it is preferable as a recycling system of unnecessary materials.

Claims (4)

천연목재, 비천연물질이 부착된 건축폐재 또는 합성수지재 등의 불필요한 자재의 재생 시스템에 있어서,In the recycling system of unneeded materials such as natural wood, non-natural building waste or synthetic resin, 천연목재, 비천연물질이 부착된 건축폐재 또는 합성수지재 등의 불필요한 자재를 열분해하여 탄화성분을 얻기 위한 탄화로,Carbonization furnace for obtaining carbonized components by pyrolyzing unnecessary materials such as natural wood, non-natural materials, building waste or synthetic resin, 상기 불필요한 자재로부터의 기화성분을 냉각액화하기 위한 컨덴서,A condenser for cooling the vaporized component from the unnecessary material, 상기 냉각액화한 성분을 분류하여 유용물질을 추출하기 위한 증류가마 및Distillation kiln for extracting useful materials by classifying the cooled liquefied components and 불순물질이나 위험물질을 그 순수물질로서 정제하여 이용하기 위한 정류탑을 구비하는 것을 특징으로 하는 불필요한 자재의 재생 시스템.And a rectifying tower for purifying and using impurity and dangerous substances as the pure substance. 제 1 항에 있어서,The method of claim 1, 액화곤란한 기화성분을 환류하여 탄화성분을 열분해하기 위한 열원으로서 이용하기 위한 유인팬을 더 구비하는 것을 특징으로 하는 불필요한 자재의 재생 시스템.And a draw pan for use as a heat source for pyrolyzing the carbonized component by refluxing the liquefied vaporized component. 삭제delete 삭제delete
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US4153514A (en) * 1975-02-27 1979-05-08 Occidental Petroleum Corporation Pyrolysis process for solid wastes
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US5366595A (en) * 1993-05-11 1994-11-22 Padgett Michael A Mobile apparatus for pyrolyzing carbonaceous material and related method
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US5728271A (en) * 1996-05-20 1998-03-17 Rti Resource Transforms International Ltd. Energy efficient liquefaction of biomaterials by thermolysis
JPH09324179A (en) * 1996-06-05 1997-12-16 Ikunou Shigen Kaihatsu:Kk Carbonizing apparatus
JPH10310774A (en) * 1997-05-09 1998-11-24 Toshio Maezato Carbonizing oven and carbonizing unit
US6861569B2 (en) * 2001-01-19 2005-03-01 Chevron U.S.A. Inc. Processes for the purification of higher diamondoids and compositions comprising such diamondoids

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