• 제목/요약/키워드: CO gas adsorption

검색결과 172건 처리시간 0.025초

함침농도와 CO2 가스 유입농도에 따른 활성탄의 흡착특성 (Adsorption Characteristics of Activated Carbons According to Impregnation Concentrations and Inlet CO2 Gas Concentrations)

  • 이동환;감상규;이송우;이민규
    • 한국환경과학회지
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    • 제19권12호
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    • pp.1403-1407
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    • 2010
  • The adsorption characteristics of $CO_2$ gas on impregnated activated carbons with MEA (Mono-ethanolamine) and AMP (2-Amino 2-methyl 1-propanol) were studied to improve the adsorption ability of $CO_2$ gas on activated carbon. The equilibrium adsorption capacity of $CO_2$ gas was increased by increment of impregnation concentration up to 40 %, but decreased above 50 %. The adsorption capacity of activated carbon impregnated with AMP was higher than activated carbon impregnated with MEA. The breakthrough was fast according to increment of inlet concentration of $CO_2$ gas.

Na2CO3, K2CO3 및 Li2CO3 첨착활성탄을 이용한CO2 제거 -고정층 반응기에서의 CO2 흡착특성- (Removal CO2 Using Na2CO3, K2CO3 and Li2CO3 Impregnated Activated Carbon -Characteristics of CO2 Adsorption in Fixed Bed Reactor-)

  • 최원준;정종현
    • 한국환경보건학회지
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    • 제34권3호
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    • pp.240-246
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    • 2008
  • The purpose of this study was to gain basic information on the characteristics of $CO_2$ adsorption in relation to $Na_2CO_3$, $K_2CO_3$, $Li_2CO_3$-impregnated activated carbon in a Fixed Bed Reactor. From the results of this study the following conclusions were made: $Na_2CO_3$, $K_2CO_3$, $Li_2CO_3$-impregnated activated carbon had a longer breakthrough time and more enhanced adsorption capacity than activated carbon alone. When tested with isothermal adsorption and tested for $CO_2$ adsorption the amount of $CO_2$ adsorbed varied with temperature, $CO_2$ inlet concentration, gas flow rate, aspect ratio, etc. Based on the results, when Langmuir, Freundlich and Dubinin-Polanyi adsorption isotherms were used for linear regression of isothermal adsorption data, Langmuir adsorption isotherm was the most suitable. And, the optimum condition for $Na_2CO_3$ and $K_2CO_3$ impregnated activated carbon make-up was 1N and $Li_2CO_3$ was 0.1N. It could be concluded that adsorption capacity was decreased with adsorption temperature and increased gas concentration. When the aspect ratio (L/D) was varied 0.5, 1.0 and 2.0, the significant drop of adsorption amount was observed below 1.0 and breakthrough time was shortened with gas flow rate.

흡착에 의한 석탄암체의 부피변화가 고려된 흡착모델 개선 및 부피변형률 예측 (Development of Volume Modified Sorption Model and Prediction for Volumetric Strain of Coal Matrix)

  • 김상진;성원모
    • 한국가스학회지
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    • 제19권2호
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    • pp.37-44
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    • 2015
  • 본 연구에서는 CBM의 1차 생산뿐 아니라 $CO_2$$N_2$ 주입을 통한 ECBM, 혹은 지중저장을 목적으로 석탄층에 $CO_2$를 주입할 때 발생할 수 있는 암체의 부피변화 영향을 고려하여 기존의 Langmuir 흡착 관계식을 개선하였다. 본 모델의 검증을 위해 $CO_2$$CH_4$, $N_2$의 단일성분 흡착실험 데이터에 기존 Langmuir 모델값과 본 모델의 결과값을 비교하였다. 그 결과, 기존 모델에서는 흡착용량이 큰 석탄일수록, 흡착친화도가 큰 가스일수록 실험값과 모델값 사이의 오차가 커지는 경향이 나타났지만 본 모델에서는 모든 조건에서 실험결과를 잘 묘사하였고 본 모델을 통해 예측한 부피변형률 역시 실험값과 유사함을 확인하였다. 이렇게 개선된 단일성분 흡착모델을 혼합가스의 흡착모델인 IAS 모델에 적용하여 부피변화가 고려된 IAS모델로 개선하였다. 그 결과 혼합가스에 대한 흡착거동 역시 기존 모델에 비해 정확도를 높였고 이는 Hall 등(1994)이 수행한 혼합가스의 흡착실험결과와의 매칭을 통해 확인하였다.

Pressure Swing Adsorption 기반 수소정제용기 3차원 모델링 및 타당성 검증 연구 (Pressure Swing Adsorption Based Hydrogen Purification Vessel 3D Modeling and Feasibility Study)

  • 차요한;최재유;주현철
    • 한국수소및신에너지학회논문집
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    • 제32권4호
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    • pp.197-204
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    • 2021
  • Pressure swing adsorption is a purification process which can get pure hydrogen. The purification process is composed of four process: compression, adsorption, desorption and discharge. In this study the adsorption process was simulated by using the Fluent and validated with experimental results. A gas used in experiment is composed of H2, CO2, CH4, and CO. Adsorption process conducted under 313 kelvin and 3 bar and bituminous-coal-based (BPL) activated carbon was used as the adsorbent. Langmuir model was applied to explain the gas adsorption. And diffusion of all the gases was controlled by micro-pore resistances. The result shows that, the most adsorbed gas was carbon dioxide, followed by methane and carbon monoxide. And carbon monoxide took the least amount of time to reach the maximum adsorption amount. The molar fraction of the off-gas became the same as the molar fraction of the gas supplied from the inlet after adsorption reached the equilibrium.

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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제올라이트: 압력순환형 흡착제로서의 특성과 CO2 흡착성능 (Zeolites: Their Features as Pressure Swing Adsorbents and CO2 Adsorption Capacity)

  • 김문현;조일흠;최상옥;추수태
    • 한국환경과학회지
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    • 제23권5호
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    • pp.943-962
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    • 2014
  • Industrial gas drying, dilute gas mixtures purification, air fractionation, hydrogen production from steam reformers and petroleum refinery off-gases, etc are conducted by using adsorptive separation technology. The pressure swing adsorption (PSA) has certain advantages over the other methods, such as absorption and membrane, that are a low energy requirement and cost-effectiveness. A key component of PSA systems is adsorbents that should be highly selective to a gas being separated from its mixture streams and have isotherms suitable for the operation principle. The six standard types of isotherms have been examined in this review, and among them the best behavior in the adsorption of $CO_2$ as a function of pressure was proposed in aspects of maximizing a working capacity upon excursion between adsorption and desorption cycles. Zeolites and molecular sieves are historically typical adsorbents for such PSA applications in gas and related industries, and their physicochemical features, e.g., framework, channel structure, pore size, Si-to-Al ratio (SAR), and specific surface area, are strongly associated with the extent of $CO_2$ adsorption at given conditions and those points have been extensively described with literature data. A great body of data of $CO_2$ adsorption on the nanoporous zeolitic materials have been collected according to pressure ranges adsorbed, and these isotherms have been discussed to get an insight into a better $CO_2$ adsorbent for PSA processes.

KOH-activated graphite nanofibers as CO2 adsorbents

  • Yuan, Hui;Meng, Long-Yue;Park, Soo-Jin
    • Carbon letters
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    • 제19권
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    • pp.99-103
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    • 2016
  • Porous carbons have attracted much attention for their novel application in gas storage. In this study, porous graphite nano-fiber (PGNFs)-based graphite nano fibers (GNFs) were prepared by KOH activation to act as adsorbents. The GNFs were activated with KOH by changing the GNF/KOH weight ratio from 0 through 5 at 900℃. The effects of the GNF/KOH weight ratios on the pore structures were also addressed with scanning electron microscope and N2 adsorption/desorption measurements. We found that the activated GNFs exhibited a gradual increase of CO2 adsorption capacity at CK-3 and then decreased to CK-5, as determined by CO2 adsorption isotherms. CK-3 had the narrowest micropore size distribution (0.6–0.78 nm) among the treated GNFs. Therefore, KOH activation was not only a significant method for developing a suitable pore-size distribution for gas adsorption, but also increased CO2 adsorption capacity as well. The study indicated that the sample prepared with a weight ratio of ‘3’ showed the best CO2 adsorption capacity (70.8 mg/g) as determined by CO2 adsorption isotherms at 298 K and 1 bar.

K계열 함침 탄소계 흡착제의 실내 저농도 이산화탄소 흡착성능 강화 (Development of Potassium Impregnated Carbon Absorbents for Indoor CO2 Adsorption)

  • 정세은;;이유리;원유섭;김재영;장재준;김하나;조성호;박영철;남형석
    • Korean Chemical Engineering Research
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    • 제60권4호
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    • pp.606-612
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    • 2022
  • 실내 거주 시간이 늘어나면서 발생하는 CO2를 인체에 무해한 농도인 1,000 ppmCO2 이하로 유지하기 위해 연구들이 활발히 진행 중이다. 본 연구에서는 저농도 CO2흡착제로서 KOH와 K2CO3와 같은 알칼리성 첨가제를 상용 활성탄에 함침하여 사용하였다. 흡착된 CO2 양은열중량분석기(TGA)와 chamber(CO2 IR analyzer)로평가하였다. 비표면적이 928.5 m2/g인 상용 활성탄(AC)은 KOH가 함침 된 KOH/AC(13.6 m2/g)와 K2CO3가 함침 된 K2CO3/AC(288.8 m2/g)보다 비표면적이 높았다. 챔버실험결과, AC는 CO2를 거의 흡착하지 않았지만, KOH/AC와 K2CO3/AC는 각각 93.5 mgCO2/gsample 및 94.5 mgCO2/gsample 흡착하였다. 이것은 비표면적 및 미세기공의 부피에 의한 물리적인 흡착 영향보다 알칼리성 활성점의 증가가 CO2 흡착에 더 유리하게 작용한 것으로 판단된다. KOH/AC와 K2CO3/AC의 재생성능은 chamber test 결과 대조군(K2CO3/Al+Si supports)과 비교했을 때 안정적으로 흡착 성능을 유지하는 것으로 나타났다(3회 반복 실험). 또한, KOH/AC와 K2CO3/AC는열중량분석기의절대습도 1%H2O를고려한조건에서 145.7 mgCO2/gsample및 150 mgCO2/gsample로 나타났다. 따라서 KOH 및 K2CO3 등과 같은 알칼리 성분의 함침은 상용 활성탄의 안정적인 흡착 및 재생 후 흡착성능을 나타내어, 실내 이산화탄소 저감을 위한 흡착제 개발에 적용될 수 있을 것으로 판단된다.

Comparison of CO on Carbon-supported Pt Catalysts Prepared by CO Gas Bubbling and Methanol Dehydrogenation

  • Han, Kee-Sung;Hwang, Ki-Ju;Han, Oc-Hee
    • Bulletin of the Korean Chemical Society
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    • 제28권12호
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    • pp.2442-2444
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    • 2007
  • CO adsorbates on the surface of Pt supported on carbon catalysts (Pt/C) were investigated by CO stripping voltammetry. Three types of CO adsorbed samples were prepared: by methanol dehydrogenation only (COm), by CO gas bubbling only (COg), and by methanol dehydrogenation followed by CO gas bubbling (COm+g). Our coverage data show that CO gas can be adsorbed on Pt/C catalyst already saturated with CO adsorbates by methanol dehydrogenation. The COm+g sample showed the properties of both COm as well as COg samples in terms of the potential although the CO adsorbed by dehydrogenation was completely exchanged with CO in the electrolyte solution. Therefore, the oxidation pathways of CO on Pt/C were observed to depend on the initial adsorption conditions of CO more strongly than on the CO coverage. Our results imply that an initial CO poisoning condition in fuel cell operation is an important factor to determine the difficulty in removing the adsorbed CO and confirm that the properties of the adsorbed CO do not change even with chemical replacement with CO in different conditions. In addition, our results indicate a low CO surface mobility on the Pt in an electrolyte solution.