• 제목/요약/키워드: Gas adsorption efficiency

검색결과 125건 처리시간 0.032초

천연가스 개질 방식 중소형 고순도 수소제조 장치 개발 연구 (Study on the development of small-scale hydrogen production unit using steam reforming of natural gas)

  • 서동주;주국택;정운호;박상호;윤왕래
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2009년도 춘계학술대회 논문집
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    • pp.720-722
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    • 2009
  • This work is mainly focused at developing the hydrogen production unit with the capacity of 20 $Nm^3/h$ of high purity hydrogen. At present steam reforming of natural gas is the preferable method to produce hydrogen at the point of production cost. The developed hydrogen production unit composed of natural gas reformer and pressure swing adsorption system. To improve the thermal efficiency of steam reforming reactor, the internal heat recuperating structure was adopted. The heat contained in reformed gas which comes out of the catalytic beds recovered by reaction feed stream. These features of design reduce the fuel consumption into burner and the heat duty of external heat exchangers, such as feed pre-heater and steam generator. The production rate of natural gas reformer was 41.7 $Nm^3/h$ as a dryreformate basis. The composition of PSA feed gas was $H_2$ 78.26%, $CO_2$ 18.49%, CO 1.43% and $CH_4$ 1.85%. The integrated production unit can produce 21.1 $Nm^3/h$ of high-purity hydrogen (99.997%). The hydrogen production efficiency of the developed unit was more than 58% as an LHV basis.

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Adsorption and Desorption Characteristics of Methyl iodide on Silver ion-Exchanged Synthetic Zeolite at High Temperature

  • Park, Geun-Il;Park, Byung-Sun;Cho, Il-Hoon;Kim, Joon-Hyung;Ryu, Seung-Kon
    • Nuclear Engineering and Technology
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    • 제32권5호
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    • pp.504-513
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    • 2000
  • The adsorption characteristics of methyl iodide generated from the simulated off-gas stream on various adsorbents such as silver ion-exchanged zeolite (AgX), zeocarbon and activated carbon were investigated. An extensive evaluation was made on the optimal silver ion-exchanged level for the effective removal of methyl iodide at temperature up to 38$0^{\circ}C$. The degree of adsorption efficiency of methyl iodide on silver ion-exchanged zeolite is strongly dependent of silver ion-amount and process temperature. The influence of temperature, methyl iodide concentration and silver ion-exchanged level on the adsorption efficiency is closely related to the pore characteristics of adsorbents. It would be facts that the effective silver ion-exchanged level was about 10 wt%, based on the degree of silver utilization for the removal of methyl iodide.

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Web Spray 법을 이용한 복합 양이온교환섬유의 제조 및 암모니아 흡착특성 (Preparation of Hybrid Cation Ion Exchange Fibers by Web Spray and Their Adsorption Properties for Ammonia Gas)

  • 박승욱;이후근;이영우;정부영;황택성
    • 폴리머
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    • 제31권6호
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    • pp.479-484
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    • 2007
  • 본 연구는 점착제 분사방식으로 고성능 hybrid ion exchange fiber(HIEF)를 제조하고 이들의 암모니아 흡착성능 및 기본물성을 측정하였다. HIEF의 이온교환용량은 수지 부착량이 증가함에 따라 증가하였으며 단일 수지와 이온교환섬유의 이온교환용량보다 크게 나타났다. 또한 암모니아의 제거율은 HIEF의 충전밀도가 증가할수록 증가하였으며 흡착 파과시간은 270분으로 섬유나 수지에 비해 길게 나타났고 최대 암모니아 흡착량은 94%이었다. 또한 암모니아 흡착 파과시간은 유량 및 농도가 증가함에 따라 빠르게 진행되었다. 암모니아 반응속도 상수(k)는 유입되는 가스농도의 증가에 따라 증가하였으며, 질량이 증가할수록 감소하였으며 가스 유속이 증가할수록 반응속도 상수(k)가 증가하였다.

흡착제를 이용한 매립지가스 내 $CO_2$ 분리 특성 (Characterization of $CO_2$ Separation in Landfill Gas by Using Adsorbent)

  • 허려화;유영돈;김문현;김형택;최익환
    • 신재생에너지
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    • 제5권4호
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    • pp.46-51
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    • 2009
  • The purpose of this study is to investigate selective adsorption of $CO_2$ from LFG (Landfill gas) by using commercialized NaX-type zeolite adsorbent under the ambient temperature and pressure. The experiment of $CO_2$ adsorption was carried out by using simulated LFG. The $CO_2$ adsorption capacity and separation efficiency of NaX-type adsorbent were investigated by analyzing gas flow rate and gas composition at inlet and outlet of the adsorption reactor. The adsorbed $CO_2$ were desorbed under decompression condition which 0.5 Torr or by air purge. Through the result to use simulated LFG, when the method of VSA was used, 73.2~75.3 mg of $CO_2$ was adsorbed per 1 g commercial adsorbent, when the method of air purge was used, 78.4~83.2 mg of $CO_2$ was adsorbed per 1 g of commercial adsorbent.

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불소화 처리된 페놀계 활성탄소를 이용한 톨루엔 가스흡착 특성 (Adsorption Characteristics of Toluene Gas Using Fluorinated Phenol-based Activated Carbons)

  • 김민지;정민정;김민일;최석순;이영석
    • 공업화학
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    • 제26권5호
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    • pp.587-592
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    • 2015
  • 휘발성 유기화합물(Volatile organic compounds, VOCs) 중 톨루엔 가스의 흡착특성을 향상시키기 위하여 불소화 반응을 이용하여 활성탄소를 처리하였다. 이 활성탄소의 기공특성과 표면특성 평가를 위하여 비표면적 측정기와 X선광전자분광법(XPS)을 사용하여 분석하였고, 가스크로마토그래피를 이용하여 톨루엔 가스 흡착능과 제거효율을 고찰하였다. 100 ppm의 톨루엔 가스가 $300cm^3/min$으로 주입될 때, 불소화 처리된 활성탄소의 파과시간이 미처리 활성탄소에 비하여 약 27% 증가하였다. 0.1 g의 불소처리 활성탄소 흡착재는 19 h의 흡착시간 동안 100 ppm 농도의 톨루엔 가스를 모두 제거하였다. 이러한 실험 결과들은 톨루엔과 같은 발암성 물질을 제거하는 처리 기술로 활용될 수 있음을 보여주었다.

탄화온도 차이에 의한 목질탄화물의 흡착성 변화 (Changes of Adsorption Properties of Woody Charcoals Prepared by Different Carbonizing Temperature)

  • 조태수;안병준;최돈하
    • Journal of the Korean Wood Science and Technology
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    • 제33권3호통권131호
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    • pp.45-52
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    • 2005
  • 북양젓나무(Abies sibirica Ledeb)의 목분, 목섬유, 수피를 탄화하여 획득한 목탄의 물성과 흡착특성을 탄화온도별로 조사하였다. 전체적으로 탄화온도가 상승할수록 탄화수율은 감소하였다. 목탄의 탄소함량은 탄화온도의 상승과 함께 증가하였으나, 수소나 산소의 함량은 감소하였다. 수피탄화물은 목분 또는 목섬유 탄화물과 비교하여 탄화수율이 높게 나타났으며, 수피탄화물 내 회분함량도 상당히 높았다. 목질탄화물의 요오드흡착능은 탄화온도가 높을수록 향상되었으며, 목분이나 섬유 탄화물이 수피탄화물보다 상대적으로 높았다. 기상의 톨루엔에 대한 흡착능은 목탄 종류에 관계없이 $600^{\circ}C$에서 탄화하였을 경우 가장 높게 나타났으며, 이러한 결과는 $600^{\circ}C$에서 생산한 목탄이 비표면적과 총세공용적이 가장 크다는 사실로 쉽게 설명되어진다. 초산가스제거율은 고온탄화물일수록 크고, 암모니아 가스 제거율은 $400^{\circ}C$와 같은 저온에서 탄화한 탄화물이 높은 경향을 나타내었다. 이는 고온탄화물일수록 알칼리성을 나타내는 반면 저온탄화물은 산성을 나타내는 것에 기인하는 것으로 보인다. 따라서 목탄의 pH가 산 또는 염기성 가스 흡착능력에 큰 영향을 주는 것으로 생각된다.

어선용 디젤엔진의 배출가스 저감 필터 개발과 저감 효율 (Development and efficiency of filter device for the emission reduction from the diesel engine in fishing boat)

  • 이경훈;김상근;김성훈;양용수;박성욱
    • 수산해양기술연구
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    • 제50권1호
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    • pp.50-57
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    • 2014
  • The performance of five kind adsorbents, which can reduce nitrogen oxide (NOx) from the diesel engine occupying 85% of the fishing boat, was carried out and the emission reduction filter was manufactured and evaluated in the adsorption efficiency of the emission gas for 240 KW diesel portable generator. As a NOx emission filter made of mordenite which has an excellent cation exchange capacity was manufactured by ball type adsorbents having excellent specific surface area. The adsorption efficiency of mordenite material applying the emission reduction filter began to show up at the operating time 10 minutes in comparison with the activated carbon and zeolite materials, and it was exposed to continue until 100% capability with passing by 20 minutes. So the adsorption efficiency of the NOx reduction filter consistently maintained at the averaged 80%.

백필터를 활용한 흡착/촉매 통합공정 시스템의 반응기 내 유동특성 및 체류시간에 대한 수치해석적 연구 (Numerical Analysis on Flow Characteristics in the Reactor of an Integrated Adsorption/Catalysis Process with Bag Filters)

  • 최청렬;구윤서
    • 한국대기환경학회지
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    • 제23권2호
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    • pp.203-213
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    • 2007
  • Numerical analysis has been performed to understand flow characteristics in the reactor with bag filters in an integrated adsorption/catalytic process which can treat dioxin and $NO_{x}$ together. Computational fluid dynamics technique was employed with Euler-Lagrangian model to consider flue gas and activated carbon particles simultaneously, so that residence time of flue gas and activated carbon particle could be obtained from the numerical analysis directly. The numerical analysis has been performed with different three particle sizes and compared each flow characteristics with particle's size. Fundamental flow patterns of flue gas and activated carbon particles, pressure distribution, residence time of flue gas and activated carbon particles, and distribution of activated carbon have been obtained from the numerical analysis. Flow patterns of flue gas and activated carbon particles in the reactor were very complicated and they moved along very various paths. Therefore, their residence time in the reactor was also various. The results obtained would be effectively used to estimate the removal efficiency in the reactor once the residence time is combined with the reaction equation.

새집증후군 유발 벤젠가스 흡착에 미치는 활성탄소섬유의 함산소불소화 영향 (Effect of Oxyfluorination of Activated Carbon Fibers on Adsorption of Benzene Gas Causing Sick House Syndrome)

  • 임형순;김민지;공은영;정진도;이영석
    • 공업화학
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    • 제29권3호
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    • pp.312-317
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    • 2018
  • 본 연구에서는 새집증후군 원인가스 중 하나인 벤젠 가스 흡착특성을 향상시키기 위하여 활성탄소섬유에 함산소불소화 처리를 실시하였다. 함산소불소화 처리된 활성탄소섬유 표면특성 및 기공특성은 X-선광전자분광기(XPS)와 Brunauer-Emmett-Teller (BET) 분석을 통해 확인하였으며, 벤젠 가스 흡착 특성은 가스크로마토그래피(GC)로 평가하였다. XPS 결과로부터 불소분압이 증가함에 따라 활성탄소섬유 표면의 불소관능기가 증가함을 알 수 있었다. 함산소불소화 처리 후 모든 샘플의 비표면적은 감소하였으나, 불소 분압이 0.1 bar일 때 그 미세기공 부피비가 증가하였다. 함산소불소화 처리된 활성탄소섬유는 11 h 동안 100 ppm의 벤젠 가스를 모두 흡착하였으며, 이는 미처리 활성탄소섬유와 비교하여 벤젠 가스 흡착효율이 약 2배 향상됨을 알 수 있었다.

연소 배출가스의 유입방식에 따른 백필터를 활용한 흡착/촉매 통합공정 시스템 반응기 내 유동특성 (Flow Characteristics with Inflow-Duct Types in the Reactor of an Integrated Adsorption/Catalysis Process with Bag Filters)

  • 최청렬
    • 대한기계학회논문집B
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    • 제31권5호
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    • pp.425-434
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    • 2007
  • An integrated adsorption/catalytic process has been considered to treat dioxin and $NO_x$ simultaneously. The process consists of a cyclone and a reactor with nine bag filters. In this study, numerical analysis has been performed to understand flow characteristics with inflow-duct types in the reactor. To consider flue gas and activated carbon particles simultaneously, Euler-Lagrangian model was employed. Fundamental flow patterns of flue gas and activated carbon particles, pressure distribution and distribution of activated carbon have been obtained from the numerical analysis. Also trace length and residence time of flue gas, residence time of activated carbon particles have been calculated directly. Flow patterns of flue gas and activated carbon particles in the reactor were very complicated and they moved along very various paths. Therefore, their residence time in the reactor was also various. The flow characteristics in the reactor were strongly influenced by inflow-duct types. The results obtained would be effectively used to estimate the removal efficiency in the reactor once the residence time is combined with the reaction equation.