KR200318879Y1 - Activated carbon reproduction system for volatility organic compound exclusion - Google Patents

Activated carbon reproduction system for volatility organic compound exclusion Download PDF

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KR200318879Y1
KR200318879Y1 KR20-2003-0011741U KR20030011741U KR200318879Y1 KR 200318879 Y1 KR200318879 Y1 KR 200318879Y1 KR 20030011741 U KR20030011741 U KR 20030011741U KR 200318879 Y1 KR200318879 Y1 KR 200318879Y1
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activated carbon
receiving space
passage
space
drying
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김금영
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(주) 바두
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/34Regenerating or reactivating
    • B01J20/3416Regenerating or reactivating of sorbents or filter aids comprising free carbon, e.g. activated carbon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/34Regenerating or reactivating
    • B01J20/3483Regenerating or reactivating by thermal treatment not covered by groups B01J20/3441 - B01J20/3475, e.g. by heating or cooling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10Inorganic adsorbents
    • B01D2253/102Carbon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708Volatile organic compounds V.O.C.'s
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/80Water
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents

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  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Treating Waste Gases (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

본 고안은, 1쌍의 망상커버(11) 사이에 호퍼 형상의 활성탄수용공간(12)이 형성되고 활성탄수용공간(12)의 하부에 수평이동통로(14)가 연통되게 형성되어 있음과 함께 수평이동통로(14)는 수직이동통로(15)와 연통되어 있고 수직이동통로(15)는 활성탄수용공간(12) 상부에 형성된 수평이동통로(16)와 연통되어 있는 하우징(1)과, 하우징(1)의 활성탄수용공간(12)에 수용되어 있는 활성탄(2)과, 활성탄수용공간(12) 하부의 수평이동통로(14)와 수직이동통로(15)에 구비되어 있는 활성탄상승수단(3)과, 활성탄수용공간(12) 상부에 형성된 수평이동통로(16)에 구비된 활성탄건조수단(4)을 포함하며, 활성탄수용공간에 수용된 활성탄에 의해 배출가스 중의 VOC 및 습기가 흡수됨과 함께 활성탄수용공간에 수용된 활성탄은 활성탄상승수단에 의해 활성탄수용공간 상부의 수평이동통로로 이동한 후 활성탄건조수단에 의해 건조되어 활성탄수용공간으로 이동하도록 된 것을 특징으로 한다.According to the present invention, a hopper-shaped activated carbon receiving space 12 is formed between a pair of reticular covers 11 and a horizontal moving passage 14 is formed at the lower portion of the activated carbon receiving space 12 so as to communicate with each other. The movement passage 14 is in communication with the vertical movement passage 15 and the vertical movement passage 15 is in communication with the horizontal movement passage 16 formed at the upper portion of the activated carbon receiving space 12, and the housing ( Activated carbon 2 accommodated in the activated carbon receiving space 12 of 1), and activated carbon raising means 3 provided in the horizontal moving passage 14 and the vertical moving passage 15 below the activated carbon receiving space 12. And activated carbon drying means (4) provided in the horizontal moving passage (16) formed above the activated carbon receiving space (12), and the activated carbon contained in the activated carbon containing space absorbs VOC and moisture in the exhaust gas. The activated carbon contained in the space is horizontally above the activated carbon storage space by the activated carbon raising means. After moving to a pain is dried by the activated carbon drying means characterized in that the activated carbon receiving space to move in.

Description

휘발성 유기화합물 제거용 활성탄 재생장치{Activated carbon reproduction system for volatility organic compound exclusion}Activated carbon reproduction system for volatility organic compound exclusion

본 고안은 휘발성 유기화합물을 흡수 제거하는데 이용하는 활성탄을 재생하여 이용하기 위한 휘발성 유기화합물(VOC) 제거용 활성탄 재생장치에 관한 것이다.The present invention relates to an activated carbon regeneration device for removing volatile organic compounds (VOC) for regenerating and using activated carbon used to absorb and remove volatile organic compounds.

휘발성 유기화합물(이하,"VOC"라 함.)은 일산화탄소, 이산화탄소, 탄산, 금속성 탄산염 및 암노늄을 제외한 탄소화합물로 대기중에서 태양광선에 의해 질소산화물(NOX)과 광화학적 산화반응을 일으켜 지표면의 오존농도를 증가시켜 스모그 현상을 일으키는 유기화합물질이다. 대표적인 물질들로는 벤젠, 톨루엔, 프로판, 부탄, 핵산 등 광화학반응이 에탄보다 큰 318종의 물질과 이들 물질이 포함된 진증기압(True Vapor Pressure:TVP)이 1.5psia 이상인 석유확학제품 및 유기용제 등을 말한다.(단 메탄, 에탄, 메틸클로라이드, 메틸클로르포름, 클로르플로르탄소류 및 퍼플로르탄소류 등 광화학적반응성이 낮은 화합물은 제외한다.)Volatile organic compounds (hereinafter referred to as "VOC") are carbon compounds, excluding carbon monoxide, carbon dioxide, carbonic acid, metallic carbonates and ammonium, which cause photochemical oxidation reactions with nitrogen oxides (NOX) in the atmosphere by sunlight. It is an organic compound that causes smog by increasing ozone concentration. Representative materials include 318 kinds of photochemical reactions such as benzene, toluene, propane, butane, nucleic acid and ethane, petroleum refining products and organic solvents with True Vapor Pressure (TVP) of 1.5 psia or more. (However, compounds with low photochemical reactivity such as methane, ethane, methyl chloride, methyl chloroform, chlorofluorocarbons and perfluorocarbons are excluded.)

VOC는 산업체에서 용매로서 많이 이용되고 있을 뿐만 아니라 화학 및 제약공장, 자동차 도장부스, 플라스틱의 건조공정에서 배출되는 유기가스에 다량 함유되어 있고, 저비점 액체연료, 파라핀, 올레핀, 방향족화합물 등 우리 생활주변에서 사용되고 있는 탄화수소류들이 거의 다 여기에 해당된다 하겠다.VOC is not only widely used as a solvent in industry, but also contained in organic gas emitted from chemical and pharmaceutical factories, automobile coating booths and plastic drying processes, and it is surrounded by low-boiling liquid fuels, paraffin, olefins and aromatic compounds. Almost all hydrocarbons that are used in this are the case.

그런데 이러한 VOC는 독성 화학물질(특히 방향족화학물 및 할로겐화 탄화수소물질)일 뿐만 아니라 광화학산화물의 전구조물이고 성층권의 오존층 파괴물질이기도 하며 지구온난화에도 영향을 미치는 물질이기도 하여 VOC를 함유하고 대기중으로 방출되는 유기가스 중에서 VOC를 여과하는 것은 환경오염방지의 중요한 사항이라 하겠다.However, these VOCs are not only toxic chemicals (especially aromatic chemicals and halogenated hydrocarbons), but also the entire structure of photochemical oxides, the stratospheric ozone depleting substances, and substances that affect global warming. Filtration of VOCs in organic gas is an important point in preventing environmental pollution.

도 6은 VOC 여과장치(100)를 자동차 도장부스(AB)에 있어서 배풍기(AB') 내의 배기통로에 설치하고 있는 것을 일 실시예로 도시하고 있고, 도 7은 종래에 이용되고 있는 VOC 여과장치(100)의 사시도를 도시하고 있다.FIG. 6 shows that the VOC filtration device 100 is installed in the exhaust passage in the air blower AB 'in the automobile coating booth AB in one embodiment, and FIG. 7 is a conventional VOC filtration device. A perspective view of 100 is shown.

종래에 제공된 VOC 여과장치(100)는 대부분의 경우 유입측과 배출측이 망상부재(120)로 커버된 함체(110) 내에 활성탄(130)이 채워진 구조로 되어 있고 이러한 VOC 여과장치(100)는 VOC를 배출하는 각종 산업용기기의 배기관(140)에 설치된다.The conventionally provided VOC filtering device 100 has a structure in which the activated carbon 130 is filled in the housing 110 in which the inlet side and the outlet side are covered with the reticular member 120 in most cases, and the VOC filtering apparatus 100 is It is installed in the exhaust pipe 140 of various industrial equipment for discharging the VOC.

상기에서 활성탄은 목재, 갈탄, 이탄(泥炭) 등을 활성화제인 염화아연이나 인산과 같은 약품으로 처리하여 건조시키거나 목탄을 수증기로 활성화시켜 가루 또는 입자 상태로 제조한 것이고, 이러한 활성탄은 주로 흡착제로서 기체나 습기를 흡수하거나 그 밖에 용제(溶劑)의 회수, 가스의 정제 또는 탈색의 기능을 발휘하는 것으로 알려져 있다.Activated carbon is prepared by treating wood, lignite, peat, etc. with chemicals such as zinc chloride or phosphoric acid as an activator, and drying or activating charcoal with water vapor to produce powder or granules. It is known to absorb gas and moisture, or to perform a function of recovery of solvent, purification of gas, or decolorization.

종래의 VOC 여과장치(100)에 의해 배출가스 중의 VOC가 여과되는 과정은 배출가스가 배기관(140)을 통하여 배출되면서 VOC 여과장치(100)의 활성탄(130)을 통과하면 배출가스 중의 VOC 및 습기가 활성탄(130)에 흡수되어 여과된다.In the process of filtering the VOC in the exhaust gas by the conventional VOC filtration device 100, when the exhaust gas is discharged through the exhaust pipe 140 and passes through the activated carbon 130 of the VOC filtration device 100, VOC and moisture in the exhaust gas Is absorbed by the activated carbon 130 and filtered.

그런데 종래의 VOC 여과장치(100)는 활성탄(130)에 흡수된 VOC나 습기를 제거할 수 없는 것이므로 일정 여과시간이 경과하면 활성탄(130)의 여과기능이 상실된다. 따라서 계속하여 여과기능을 발휘하기 위하여는 새로운 활성탄(130)으로 교환해 주어야 되는 것이므로 그 교환작업이 번거로운 것이다. 더욱이 종래의 VOC 여과장치(100)는 VOC 및 습기를 여과할 뿐 근본적으로 VOC를 제거할 수는 없는 것이어서 환경오염방지에 한계가 따른다.However, since the conventional VOC filtration device 100 cannot remove VOC or moisture absorbed by the activated carbon 130, the filtration function of the activated carbon 130 is lost after a predetermined filtration time. Therefore, in order to continue to exhibit a filtration function is to be replaced with a new activated carbon 130 is a cumbersome replacement work. Moreover, the conventional VOC filtration device 100 filters VOC and moisture, but cannot fundamentally remove the VOC, thereby limiting environmental pollution.

본 고안은 상기와 같은 종래의 여러 문제점을 고려하여 고안된 것으로서, 그 목적으로 하는 것은, 활성탄을 계속하여 순환시키면서 건조시켜 활성탄에 흡착된 VOC 및 습기를 증발시키고 또 증발된 VOC 및 습기를 가열수단에 의해 가열하여 제거함으로서 완벽하게 VOC를 제거함은 물론, 특히 활성탄을 교환하지 않고 계속하여 재생하여 이용할 수 있는 VOC 제거용 활성탄 재생장치를 제공하고자 하는 것에 있다.The present invention has been devised in consideration of the above-mentioned various problems, and its object is to evaporate VOC and moisture adsorbed on activated carbon by continuously circulating activated carbon, and further evaporate VOC and moisture to heating means. The present invention aims to provide a VOC removal activated carbon regeneration apparatus that can completely remove VOCs by heating and remove them, and in particular, can continuously regenerate and use them without exchanging activated carbons.

도 1은 본 고안에 따른 활성탄 재생장치의 단면도1 is a cross-sectional view of the activated carbon recycling apparatus according to the present invention

도 2는 도 1의 A-A선 단면도2 is a cross-sectional view taken along the line A-A of FIG.

도 3은 도 1의 "B"부 확대도3 is an enlarged view of a portion “B” of FIG. 1;

도 4는 도 2의 "C"부 확대도4 is an enlarged view of a portion “C” of FIG. 2;

도 5는 도 3의 D-D선 확대도5 is an enlarged view of the D-D line of FIG.

도 6은 VOC 여과장치를 자동차 도장부스에 있어서 배풍기 내의 배기통로에 설치한 상태도Fig. 6 is a state diagram in which the VOC filtration device is installed in the exhaust passage of the exhaust fan in an automobile paint booth.

도 7은 종래에 이용되고 있는 VOC 여과장치의 사시도7 is a perspective view of a conventional VOC filtration device;

〈도면중 주요 부분에 대한 부호설명〉<Description of Signs of Major Parts of Drawings>

1. 하우징 --- 11. 망상커버, 12. 활성탄수용공간, 13. 배출구멍1. Housing --- 11. Reticular cover, 12. Space for activated carbon, 13. Outlet

14, 16. 수평이동통로, 15. 수직이동통로,14, 16. horizontal passage, 15. vertical movement passage,

2. 활성탄2. Activated Carbon

3. 활성탄상승수단 --- 31, 33. 모터, 32. 이송스크류, 34. 버??컨베어3. Activated carbon lift means --- 31, 33. Motor, 32. Feed Screw, 34. Burr Conveyor

4. 활성탄건조수단 --- 41. 이송스크류, 42. 건조롤러, 43.히팅바4. Activated carbon drying means --- 41. Transfer screw, 42. Drying roller, 43. Heating bar

45. 오일45. Oil

5. 구동수단5. Driving means

본 고안에서 제공하는 VOC 제거용 활성탄 재생장치는, 1쌍의 망상커버 사이에 호퍼 형상의 활성탄수용공간이 형성되고 활성탄수용공간의 하부에 수평이동통로가 연통되게 형성되어 있음과 함께 수평이동통로는 수직이동통로와 연통되어 있고 수직이동통로는 활성탄수용공간 상부에 형성된 수평이동통로와 연통되어 있는 하우징과, 하우징의 활성탄수용공간에 수용되어 있는 활성탄과, 활성탄수용공간 하부의 수평이동통로와 수직이동통로에 구비되어 있는 활성탄상승수단과, 활성탄수용공간 상부에 형성된 수평이동통로에 구비된 활성탄건조수단를 포함하는 것을 특징으로 한다.The activated carbon regeneration device for VOC removal according to the present invention includes a hopper-shaped activated carbon receiving space formed between a pair of reticular covers and a horizontal moving passage formed at a lower portion of the activated carbon receiving space. The vertical movement passage is in communication with the vertical movement passage and the vertical movement passage communicates with the horizontal movement passage formed at the upper portion of the activated carbon receiving space, the activated carbon contained in the activated carbon receiving space of the housing, and the vertical movement passage and the vertical movement passage under the activated carbon receiving space Activated carbon rising means provided in the passage, and activated carbon drying means provided in the horizontal movement passage formed on the upper space for the activated carbon receiving space.

상기와 같은 본 고안은, 활성탄수용공간에 수용된 활성탄에 의해 배출가스 중의 VOC 및 습기가 흡수된다. 그리고 활성탄수용공간에 수용된 활성탄은 활성탄상승수단에 의해 활성탄수용공간 상부의 수평이동통로로 이동한 후 활성탄건조수단에 의해 건조되어 활성탄수용공간으로 이동한다.The present invention as described above, VOC and moisture in the exhaust gas is absorbed by the activated carbon contained in the activated carbon receiving space. The activated carbon contained in the activated carbon storage space is moved to the horizontal moving passage above the activated carbon storage space by the activated carbon raising means and then dried by the activated carbon drying means to move to the activated carbon storage space.

따라서 본 고안은 활성탄을 계속하여 순환시키면서 건조시켜 활성탄에 흡착된 VOC 및 습기를 증발시키고 또 증발된 VOC 및 습기를 별도의 가열수단에 의해 가열하여 제거함으로서 완벽하게 VOC를 제거한다. 특히 활성탄을 교환하지 않고 계속 재생하여 이용함으로서 효율적으로 연속하여 VOC를 제거한다.Therefore, the present invention continuously circulates the activated carbon while drying to evaporate the VOC and moisture adsorbed on the activated carbon, and remove the VOC completely by heating and removing the vaporized VOC and moisture by separate heating means. In particular, by continuously regenerating and using the activated carbon, the VOC is continuously removed efficiently.

이하 본 고안의 구체적인 일 실시예를 도면에 따라서 상세히 설명한다.Hereinafter, a specific embodiment of the present invention will be described in detail with reference to the drawings.

도 1은 본 고안에 따른 활성탄 재생장치의 단면도, 도 2는 도 1의 A-A선 단면도를 각각 도시하고 있다.1 is a cross-sectional view of the activated carbon regeneration device according to the present invention, Figure 2 is a cross-sectional view taken along the line A-A of FIG.

하우징(1)은 사각 형상의 함체로 되어 있음과 함께 배출가스의 유입측과 배출측이 되는 측부에 각각 망상커버(11)가 설치되어 있고 망상커버(11) 사이에 호퍼 형상의 활성탄수용공간(12)이 형성되어 있다.The housing 1 is a rectangular box, and the reticular cover 11 is provided at each side of the inlet and discharge side of the discharge gas, and a hopper shaped space for active carbon between the reticular covers 11 ( 12) is formed.

활성탄수용공간(12)의 하부에는 활성탄수용공간(12)의 길이방향을 따라 배출구멍(13)이 형성되어 있으며 이 배출구멍(13)의 하부에는 수평이동통로(14)가 형성되어 있다.A discharge hole 13 is formed in the lower portion of the activated carbon receiving space 12 along the longitudinal direction of the activated carbon receiving space 12, and a horizontal movement passage 14 is formed in the lower portion of the discharge hole 13.

수평이동통로(14)의 길이방향 일측 선단부를 연통하여 상하로는 수직이동통로(15)가 형성되어 있고 수직이동통로(15)는 활성탄수용공간(12) 상부에 형성된 수평이동통로(16)와 연통되어 있다. 그리고 수평이동통로(16)의 상부에는 다수의 배출구멍(17)이 형성되어 있다.The vertical movement passage 15 is formed in the vertical movement passage 15 by communicating one end portion in the longitudinal direction of the horizontal movement passage 14, and the vertical movement passage 15 is formed with the horizontal movement passage 16 formed on the upper portion of the activated carbon receiving space 12. In communication. In addition, a plurality of discharge holes 17 are formed in the upper portion of the horizontal moving passage 16.

상기 하우징(1)의 활성탄수용공간(12)에는 배기가스 중의 VOC와 습기를 흡수하기 위한 활성탄(2)이 채워져 있다.The activated carbon receiving space 12 of the housing 1 is filled with activated carbon 2 for absorbing VOC and moisture in the exhaust gas.

하우징(1)의 수평이동통로(14)와 수직이동통로(15)에는 활성탄수용공간(12) 내의 활성탄(2)을 상측의 수평이동통로(16)로 상승시키기 위한 활성탄상승수단(3)이 구비되어 있다.In the horizontal movement passage 14 and the vertical movement passage 15 of the housing 1, activated carbon raising means 3 for raising the activated carbon 2 in the activated carbon receiving space 12 to the upper horizontal movement passage 16 is provided. It is provided.

활성탄상승수단(3)은 수평이동통로(14)를 따라 회전 가능하게 배치되어 모터(31)에 의해 구동할 수 있도록 설치된 이송스크류(32)와, 수직이동통로(15)의 상하에 걸쳐 회전 가능하게 설치되어 모터(33)에 의해 구동할 수 있도록 설치된 버??컨베어(34)로 되어 있다.Activated carbon lift means (3) is rotatably disposed along the horizontal movement passage 14 and rotatable across the vertical movement passage (15) and the transfer screw (32) installed to be driven by the motor (31). It is installed as a bucket conveyor (34) so as to be installed so that it can be driven by the motor (33).

상기와 같은 활성탄상승수단(3)은 이송스크류(32)에 의해 활성탄수용공간(12) 하부의 활성탄(2)을 수평이동통로(14)의 하부로 이송한 후 버??컨베어(34)에 의해 상승 이송하여 상측의 수평이동통로(16)로 이동시킨다.The activated carbon raising means 3 as described above transfers the activated carbon 2 in the lower portion of the activated carbon receiving space 12 to the lower portion of the horizontal moving passage 14 by the transfer screw 32 to the burr conveyor 34. By the upward movement to move to the upper horizontal movement path (16).

수평이동통로(16)에는 이송되어 온 활성탄(2)을 건조하여 활성탄(12)에 흡수된 VOC와 수분을 증발시키기 위한 활성탄건조수단(4)이 구비되어 있다.The horizontal movement passage 16 is provided with activated carbon drying means 4 for drying the transported activated carbon 2 to evaporate VOC and moisture absorbed in the activated carbon 12.

활성탄건조수단(4)은 도 3 및 도 4에 도시된 바와 같이 수평이동통로(16) 따라 회전 가능하게 배치된 이송스크류(41)와, 이송스크류(41) 하부에 회동 가능하고 평행하게 설치된 한쌍의 건조롤러(42)와, 각 건조롤러(42) 내에 구비된 히팅바(43)로 되어 있다. 여기서 이송스크류(41)와 건조롤러(42)는 그 길이방향의 양단이 하우징(1)에 회동 가능하게 설치되는 것이며 건조롤러(42) 내에 구비된 히팅바(43)는 그 길이방향의 양단이 하우징(1)에 고정된 지지브라??(44)에 고정되어 있다.Activated charcoal drying means 4 is a pair of the rotating screw disposed rotatably and parallel to the lower portion of the conveying screw 41 and the conveying screw 41 is disposed rotatably along the horizontal moving passage 16 as shown in Figs. Drying rollers 42 and a heating bar 43 provided in each drying roller 42. Here, the feed screw 41 and the drying roller 42 are both ends of the longitudinal direction rotatably installed in the housing 1 and the heating bar 43 provided in the drying roller 42 has both ends of the longitudinal direction. It is fixed to a support bra (44) fixed to the housing (1).

건조롤러(42)와 히팅바(43) 사이의 공간에는 가열용 오일(45)이 밀봉된 상태로 수용되어 있다. 여기서 오일(45)은 건조롤러(42)를 균일하고 더욱 효과적으로 가열하기 위하여 구비된다.The heating oil 45 is housed in a sealed state between the drying roller 42 and the heating bar 43. The oil 45 is provided to heat the drying roller 42 uniformly and more effectively.

활성탄건조수단(4)은 구동수단(5)에 의해 구동된다.The activated carbon drying means 4 is driven by the drive means 5.

구동수단(5)은 도 3 및 도 5에 도시된 바와 같이 모터(51)의 구동기어(52)에 치합된 이송스크류기어(53)와, 상호 치합된 한쌍의 건조롤러기어(54)와, 이송스크류기어(53)와 건조롤러기어(54)에 치합된 아이들기어(55)로 되어 있다. 이러한 구동수단(5)은 모터(51)를 작동하여 구동기어(52)를 회전시키면 이송스크류(41)에 결합된 이송스크류기어(53)가 회전하고, 각 건조롤러(42)에 결합된 한쌍의 건조롤러기어(54)가 그 대향면이 하향 회전하도록 되어 있다.As shown in FIGS. 3 and 5, the driving means 5 includes a transfer screw gear 53 engaged with the drive gear 52 of the motor 51, a pair of dry roller gears 54 engaged with each other, An idle gear 55 meshed with the transfer screw gear 53 and the dry roller gear 54 is used. When the driving means 5 rotates the drive gear 52 by operating the motor 51, the transfer screw gear 53 coupled to the transfer screw 41 rotates, and a pair coupled to each drying roller 42. Of the dry roller gear 54 is formed so that its opposite surface rotates downward.

상기 활성탄건조수단(4)은 활성탄상승수단(3)에 의해 수평이동통로(16)로 이송된 활성탄(12)을 이송스크류(41)에 의해 한쌍의 건조롤러(42) 사이로 균일하게 이송하며 이와 같이 이송되는 활성탄(2)은 회전하는 한쌍의 건조롤러(42) 사이를통과하면서 건조롤러(42)에 의해 가열 건조된 후 활성탄수용공간(12)으로 낙하하도록 되어 있다. 여기서 활성탄(2)의 가열 건조과정에서는 활성탄(2)에 흡수된 VOC 및 수분이 증발하여 분리되며 분리된 VOC 및 수분은 배출구멍(17)을 통하여 배출된 후 별도의 고온 가열수단에 의해 가열되어 제거된다.The activated carbon drying means 4 uniformly transfers the activated carbon 12 transferred to the horizontal moving passage 16 by the activated carbon raising means 3 between the pair of drying rollers 42 by the transfer screw 41. The activated carbon 2 to be conveyed together is heated and dried by the drying roller 42 while passing through a pair of rotating drying rollers 42 to fall into the activated carbon receiving space 12. Here, in the heating and drying process of the activated carbon 2, VOC and moisture absorbed by the activated carbon 2 are separated by evaporation, and the separated VOC and moisture are discharged through the discharge hole 17 and then heated by a separate high temperature heating means. Removed.

상기와 같은 본 고안은 종래와 같이 VOC를 배출하는 각종 산업용기기의 배기관(6)에 설치되며 활성탄(2)에 의해 VOC를 흡수하고 활성탄(2)을 재생하는 과정은 다음과 같다.The present invention as described above is installed in the exhaust pipe (6) of the various industrial equipment for discharging the VOC as conventionally, the process of absorbing the VOC by the activated carbon (2) and regenerating the activated carbon (2) is as follows.

본 고안은 배출가스가 배기관(6)을 통해 활성탄수용공간(12)에 수용된 활성탄(2)을 통과하면 이 과정에서 배출가스 중의 VOC 및 습기가 활성탄(2)에 흡수된다.According to the present invention, when the exhaust gas passes through the activated carbon 2 accommodated in the activated carbon receiving space 12 through the exhaust pipe 6, VOC and moisture in the exhaust gas are absorbed by the activated carbon 2 in this process.

한편, 활성탄수용공간(12)에 수용된 활성탄(2)은 이송스크류(32)에 의해 버??컨베어(34)의 하부로 이동하여 버??컨베어(34)에 의해 활성탄수용공간(12) 상부의 수평이동통로(16)로 이송된다.On the other hand, the activated carbon 2 accommodated in the activated carbon receiving space 12 is moved to the lower portion of the buffer conveyor 34 by the transfer screw 32, the upper portion of the activated carbon receiving space 12 by the buffer conveyor 34 Is transferred to the horizontal movement path (16).

수평이동통로(16)로 이송된 활성탄(2)은 이송스크류(41)에 의해 한쌍의 건조롤러(42) 사이로 고르게 공급되고, 이어서 회전하는 건조롤러(42)를 통과하는 과정에서 건조되어 활성탄수용공간(12)으로 회수된다. 여기서 활성탄(2)의 건조 과정에서는 활성탄(2)에 흡수되어 있는 VOC 및 수분이 활성탄(2)으로부터 증발하여 활성탄(2)으로부터 분리되며 분리된 VOC 및 수분은 배출구멍(17)을 통하여 배출된 후 별도의 고온 가열수단에 의해 가열되어 제거된다.The activated carbon 2 transferred to the horizontal moving passage 16 is evenly supplied between the pair of drying rollers 42 by the transfer screw 41, and then dried in the process of passing through the rotating drying rollers 42 for active carbon water. It is recovered to the space 12. In the drying process of the activated carbon 2, VOC and moisture absorbed in the activated carbon 2 are separated from the activated carbon 2 by evaporation from the activated carbon 2, and the separated VOC and water are discharged through the discharge hole 17. After being heated and removed by a separate high temperature heating means.

본 고안은, 활성탄수용공간에 수용된 활성탄에 의해 배출가스 중의 VOC 및 습기가 흡수된다. 그리고 활성탄수용공간에 수용된 활성탄은 활성탄상승수단에 의해 활성탄수용공간 상부의 수평이동통로로 이동한 후 활성탄건조수단에 의해 건조되어 활성탄수용공간으로 이동한다.The present invention absorbs VOC and moisture in the exhaust gas by the activated carbon contained in the activated carbon storage space. The activated carbon contained in the activated carbon storage space is moved to the horizontal moving passage above the activated carbon storage space by the activated carbon raising means and then dried by the activated carbon drying means to move to the activated carbon storage space.

따라서 본 고안은 활성탄을 계속하여 순환시키면서 건조시켜 활성탄에 흡착된 VOC 및 습기를 증발시키고 또 증발된 VOC 및 습기를 별도의 가열수단에 의해 가열하여 제거함으로서 완벽하게 VOC를 제거한다. 특히 본 고안은 활성탄을 교환하지 않고 계속 건조 재생하여 이용할 수 있다.Therefore, the present invention continuously circulates the activated carbon while drying to evaporate the VOC and moisture adsorbed on the activated carbon, and remove the VOC completely by heating and removing the vaporized VOC and moisture by separate heating means. In particular, the present invention can be used by continuing to dry regeneration without replacing the activated carbon.

Claims (4)

1쌍의 망상커버(11) 사이에 호퍼 형상의 활성탄수용공간(12)이 형성되고 활성탄수용공간(12)의 하부에 수평이동통로(14)가 연통되게 형성되어 있음과 함께 수평이동통로(14)는 수직이동통로(15)와 연통되어 있고 수직이동통로(15)는 활성탄수용공간(12) 상부에 형성된 수평이동통로(16)와 연통되어 있는 하우징(1)과, 하우징(1)의 활성탄수용공간(12)에 수용되어 있는 활성탄(2)과, 활성탄수용공간(12) 하부의 수평이동통로(14)와 수직이동통로(15)에 구비되어 있는 활성탄상승수단(3)과, 활성탄수용공간(12) 상부에 형성된 수평이동통로(16)에 구비된 활성탄건조수단(4)을 포함하며, 활성탄수용공간에 수용된 활성탄에 의해 배출가스 중의 VOC 및 습기가 흡수됨과 함께 활성탄수용공간에 수용된 활성탄은 활성탄상승수단에 의해 활성탄수용공간 상부의 수평이동통로로 이동한 후 활성탄건조수단에 의해 건조되어 활성탄수용공간으로 이동하도록 된 것을 특징으로 하는 휘발성 유기화합물 제거용 활성탄 재생장치.A hopper shaped activated carbon accommodating space 12 is formed between the pair of reticular covers 11, and a horizontal moving passage 14 is formed in communication with the lower portion of the activated carbon accommodating space 12. ) Is in communication with the vertical movement passage 15 and the vertical movement passage 15 is in communication with the horizontal movement passage 16 formed on the activated carbon receiving space 12, the activated carbon of the housing (1) Activated carbon 2 accommodated in the receiving space 12, activated carbon raising means 3 provided in the horizontal moving passage 14 and the vertical moving passage 15 under the activated carbon receiving space 12, and the activated carbon receiving unit Activated carbon drying means (4) provided in the horizontal moving passage 16 formed in the upper space 12, the activated carbon contained in the activated carbon storage space is absorbed VOC and moisture in the exhaust gas and activated carbon contained in the activated carbon storage space Is a horizontal movement path above the activated carbon storage space by means of activated carbon ascending means. Activated carbon is dried by drying means to remove volatile organic compounds for the activated carbon and reproducing apparatus, characterized in that the activated carbon receiving space to move after donghan. 제 1항에 있어서, 활성탄상승수단(3)은 활성탄수용공간(12) 하부의 수평이동통로(14)에 회전 가능하게 설치된 이송스크류(32)와, 수직이동통로(15)에 회전 가능하게 설치된 버??컨베어(34)로 되어, 이송스크류에 의해 수직이동통로로 이송된 활성탄이 버??컨베어에 의해 상승하여 활성탄수용공간 상부의 수평이동통로로 상승되도록 된 것을 특징으로 하는 휘발성 유기화합물 제거용 활성탄 재생장치.The method of claim 1, wherein the activated carbon lifting means (3) is rotatably installed in the vertical movement passage (15) and the transfer screw (32) rotatably installed in the horizontal movement passage (14) below the activated carbon receiving space (12) Volatile conveyor (34), the activated carbon transported in the vertical movement path by the transfer screw is lifted by the buffer conveyor to remove the volatile organic compounds, characterized in that it is raised to the horizontal movement passage in the upper portion of the activated carbon receiving space Activated carbon regeneration device. 제 1항에 있어서, 활성탄건조수단(4)은 활성탄수용공간(12) 상부의 수평이동통로(16)에 회전 가능하게 설치된 이송스크류(41)와, 이송스크류(41) 하부에 회동 가능하게 설치된 한쌍의 건조롤러(42)와, 건조롤러(42) 내에 구비된 히팅바(43)로 되어, 이송스크류에 의해 이송되는 활성탄이 한쌍의 건조롤러를 통과하는 과정에서 가열 건조된 후 활성탄수용공간으로 낙하하도록 된 것을 특징으로 하는 휘발성 유기화합물 제거용 활성탄 재생장치.The method of claim 1, wherein the activated carbon drying means (4) is rotatably installed in the transport screw 41 and the transport screw 41, which is rotatably installed in the horizontal movement passage (16) above the activated carbon receiving space (12) It consists of a pair of drying roller 42 and a heating bar 43 provided in the drying roller 42, the activated carbon conveyed by the conveying screw is heated and dried in the process of passing through the pair of drying rollers to the activated carbon receiving space Activated carbon regeneration device for removing volatile organic compounds, characterized in that the fall. 제 3항에 있어서, 건조롤러(42)와 히팅바(43) 사이에는 가열용 오일(45)이 밀봉되게 수용된 것을 특징으로 하는 휘발성 유기화합물 제거용 활성탄 재생장치.4. The activated carbon regeneration apparatus for removing volatile organic compounds according to claim 3, wherein the heating oil (45) is sealed between the drying roller (42) and the heating bar (43).
KR20-2003-0011741U 2003-04-16 2003-04-16 Activated carbon reproduction system for volatility organic compound exclusion KR200318879Y1 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101707598B1 (en) * 2015-09-21 2017-02-16 강원대학교산학협력단 Charcoal Regeneration Apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101707598B1 (en) * 2015-09-21 2017-02-16 강원대학교산학협력단 Charcoal Regeneration Apparatus
WO2017052117A1 (en) * 2015-09-21 2017-03-30 강원대학교산학협력단 Activated carbon recycling apparatus

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