• Title/Summary/Keyword: Adsorption-Desorption Behavior

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공진어드미턴스를 이용한 유기가스의 흡착패턴의 분석 (Analysis of Adsorption Pattern of Orgnaic Gas Using Resonant Admittance Method)

  • 김정명;최용성;장정수;권영수
    • 대한전기학회:학술대회논문집
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    • 대한전기학회 1996년도 하계학술대회 논문집 C
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    • pp.1565-1568
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    • 1996
  • The adsorption and desorption behavior of orgnaic gases were investigated using the resonant frequency and admittance method. Sensitive material were depositied on the quartz crystal microbalence by using Langmuir-Blodgett method. To investigate the response characteristics of organic gases, Resonant frequency-Resonant admittance (F-A) diagram was used. The quantity and quality information about organic gases can be obtained by that diagram. As a results, when the organic gases were adsorpted into sensitive material, the physical property changees of sensitive material were occured.

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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.

활성탄에서의 아세트산 흡탈착 거동 (Sorption Behavior of Acetic Acid onto Activated Carbons)

  • 이채영;정진석;신은우
    • Korean Chemical Engineering Research
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    • 제46권6호
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    • pp.1130-1134
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    • 2008
  • 아세트산은 테레프탈산 제조 공정에서 용매로 사용되며, 사용된 아세트산은 반응 후 증류 공정을 통하여 분리 회수된다. 그러나 소량의 아세트산은 그대로 폐수에 유입되어 버려지는데, 흡착공정을 이용하면 소량의 아세트산을 회수하여 다시 재사용할 수 있다. 본 연구에서는 활성탄을 아세트산 흡착제로 활용하여 상용활성탄의 아세트산 흡착능과 흡착능에 대한 온도 및 흡착제 산처리 효과를 살펴보았다. 활성탄의 아세트산 흡착능은 흡착 키네틱 실험으로 관찰한 결과, 303 K에서는 0.176 mmol/g의 흡착능을 보였으나, 343 K에서는 0.118 mmol/g으로 흡착능이 떨어졌다. 즉, 온도가 증가하면 활성탄의 아세트산 흡착능은 감소하는 결과가 나타났다. 산처리실험에서는 활성탄 표면을 염산 혹은 옥살산으로 처리할 경우, 활성탄의 아세트산 흡착능이 소폭 증가하였다. 이는 산처리로 인해 활성탄 표면에 카르복실산, 혹은 페놀 수산화기 등 표면 관능기가 증가하였기 때문인 것으로 보인다. 아세트산 탈착 실험에서는 정량분석결과, 흡착된 아세트산의 89% 정도가 탈착되었다.

토양 중 농약의 동태 (Behavior of Pesticides in Soil)

  • 이규승
    • 농약과학회지
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    • 제14권3호
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    • pp.303-307
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    • 2010
  • 총설은 1996년 "농업생태계에 대한 잔류농약의 영향평가"라는 총설 이후 국내에서 발표된 토양 중에서의 농약의 동태에 관한 연구 보문을 요약 정리한 것이다. 내용은 농약의 지표면 유출, 농약의 토양 중 흡착 및 탈착, 농약의 토양 중 용탈, 농약의 토양 종 분해는 미생물에 의한 분해와 비생물학적 분해로 나누어 검토하였고, 농약의 토양 종에서의 행적 및 토양 중 잔류와 잔류 분석법 등으로 구분하여 정리하였다.

Gas Separation of Pyrolyzed Polymeric Membranes: Effect of Polymer Precursor and Pyrolysis Conditions

  • Jung, Chul-Ho;Kim, Gun-Wook;Han, Sang-Hoon;Lee, Young-Moo
    • Macromolecular Research
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    • 제15권6호
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    • pp.565-574
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    • 2007
  • In this study, five representative, commercially available polymers, Ultem 1000 polyetherimide, Kapton polyimide, phenolic resin, polyacrylonitrile and cellulose acetate, were used to prepare pyrolyzed polymer membranes coated on a porous {\alpha}-alumina$ tube via inert pyrolysis for gas separation. Pyrolysis conditions (i.e., final temperature and thermal dwell time) of each polymer were determined using a thermogravimetric method coupled with real-time mass spectroscopy. The surface area and pore size distribution of the pyrolyzed materials derived from the polymers were estimated from the nitrogen adsorption/desorption isotherms. Pyrolyzed membranes from polymer precursors exhibited type I sorption behavior except cellulose acetate (type IV). The gas permeation of the carbon/{\alpha}-alumina$ tubular membranes was characterized using four gases: helium, carbon dioxide, oxygen and nitrogen. The polyetherimide, polyimide, and phenolic resin pyrolyzed polymer membranes showed typical molecular sieving gas permeation behavior, while membranes from polyacrylonitrile and cellulose acetate exhibited intermediate behavior between Knudsen diffusion and molecular sieving. Pyrolyzed membranes with molecular sieving behavior (e.g., polyetherimide, polyimide, and phenolic resin) had a $CO_2/N_2$ selectivity of greater than 15; however, the membranes from polyacrylonitrile and cellulose acetate with intermediate gas transport behavior had a selectivity slightly greater than unity due to their large pore size.

휘발성 유기용제가 흡착된 흡착제의 초임계 이산화탄소를 이용한 재생특성 (Regeneration Characteristics of Adsorbent Loaded with VOCs using Supercritical Carbon Dioxide)

  • 이승범;성대형;홍인권
    • 공업화학
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    • 제8권5호
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    • pp.737-741
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    • 1997
  • 휘발성 유기용제의 주된 제거방법은 흡착제를 이용한 흡착 공정이 추천된다. 본 연구에서는 입상활성탄과 활성탄소섬유에 휘발성 유기용제를 흡착시킨 후 폐흡착제를 탈착컬럼에 넣고 318.15 K의 온도에서 압력을 변수(2000~3000 psi)로 하는 초임계 이산화탄소를 이용하여 재생하였다. 초임계 이산화탄소의 압력이 증가함에 따라 탈착율과 요오드 흡착가는 증가하였으며, 재생시간은 MEK와 benzene의 경우 각각 70분과 60분이었다. 최대 탈착율은 3000psi의 압력에서 MEK가 흡착된 입상활성탄과 활성탄소섬유의 경우 각각 초기 흡착량의 64.0%, 55.3%가 탈착되었으며, 벤젠이 흡착된 입상활성탄과 활성탄소섬유의 경우에는 각각 59.1%, 45.2%가 탈착되었다. 또한 Tan과 Liou의 모델로 출구농도를 예측할 수 있었다. 따라서 입상활성탄뿐만 아니라 활성탄소섬유의 재생공정에도 초임계유체 재생법의 적응 가능성을 확인할 수 있었다.

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알루미늄합금 진공용기의 기체방출 특성 (Outgassing characteristics of an aluminum-alloy vacuum chamber)

  • 박종도;하태균;문상운;배인호;정석민
    • 한국진공학회지
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    • 제10권2호
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    • pp.164-172
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    • 2001
  • 기계가공으로 제작되고 알칼리 화학세정을 거친 알루미늄합금(A5083) 진공용기에 대한 기체방출 특성을 조사하였다. 상온배기를 시작한 후 가열탈기체 처리를 하기 전 까지 배기곡선은 ~$t^{-1.15}$ 모양을 따랐다. 이 알루미늄 진공용기에 대한 배기곡선을 비교적 간단한 모델들을 사용하여 용기의 내표면에 흡착되어 있는 물의 1차 방출로 분석하였다. ~$10^{-5}-10^{-8}$Torr 압력구간에서 물분자는 ~17 - 22 kcal/mol사이의 탈리에너지 값을 가지는 몇 개의 흡착석에서 방출됨을 알 수 있었다. 한편 $100^{\circ}C$, 24 시간 가열 탈기체 처리후 알루미늄용기에 대한 기체방출률은 상온에서 ~1$\times$$10^{-13}$ Torr$\ell$/s $\textrm{cm}^2$로 측정되었다.

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Adsorption and Thermal Reduction Mechanism of CO2 on ZnO/Cu Model Catalysts

  • Kim, Yeonwoo;Kim, Sehun
    • 한국진공학회:학술대회논문집
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    • 한국진공학회 2014년도 제46회 동계 정기학술대회 초록집
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    • pp.191.2-191.2
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    • 2014
  • Cu/ZnO/$Al_2O_3$ is widely used methanol synthesis catalyst at elevated pressures P (50 to 100 bar) and temperatures T (473 to 573 K) using $CO_2$, CO, $H_2$ syngas mixture. Although Cu step and planar defects have been regarded as active sites in this catalyst, detailed $CO_2$ hydrogenation procedure has been still unknown and debated as well as initial intermediate. In this study, we investigated the mechanism of $CO_2$ hydrogenation on Cu(111) model surface at P (1 bar) and T (298 to 450 K) using reflection absorption infrared spectroscopy (RAIRS). Two distinct formates by hydrogenation of $CO_2$, on step and on terrace, show different behavior with elevating temperature. The peak intensity of on step formate was continuously decreased above 360 K up to 450K in contrast to the increase of on terrace formate. These phenomena are strong possibilities that the formate is initial intermediate and is desorbed by hydrogenation reaction because thermal desorption temperature of formate (~470 K) is much higher than desorption of on step formate. And the formate production peak of on step site was weakly correlated with CO formation.

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부산 도심하천 하구의 Nonylphenol 거동 특성 (Behavior Characteristics of Nonylphenol in the Downstream of River in Busan, Korea)

  • 김선영;노경준;김동명
    • 한국수산과학회지
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    • 제52권1호
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    • pp.74-80
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    • 2019
  • Nonylphenol is an endocrine-disrupting chemical that is the degradation product of the nonionic surfactants nonylphenol ethoxylates. To understand the contamination and behavioral characteristics of nonylphenol, we measured the nonylphenol concentrations in surface water in the lower reaches of the Suyeong River, Korea. The results were used to estimate the material balance. The target area was divided into three regions to estimate the material balance of nonylphenol. In region 1, in flux of the dissolved nonylphenol was 282.3 g/day and the nonylphenol influx in particulate suspended solids was 1,582.8 g/day. The dissolved nonylphenol outflow discharged toward region 2 was 192.5 g/day, while the adsorption to particulate suspended solids was 89.8 g/day. Within the particulate suspended solids, the outflow to region 2 was 1,250.0 g/day, while the estimated amount settling in the sediments was 422.7 g/day. The adsorption of dissolved nonylphenol to the particulate suspended solids in regions 1 and 2 was 31.8% and 54.9%, respectively. In region 3, the desorption rate was 8.8%.

Modelling and packed bed column studies on adsorptive removal of phosphate from aqueous solutions by a mixture of ground burnt patties and red soil

  • Rout, Prangya R.;Dash, Rajesh R.;Bhunia, Puspendu
    • Advances in environmental research
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    • 제3권3호
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    • pp.231-251
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    • 2014
  • The present study examines the phosphate adsorption potential and behavior of mixture of Ground Burnt Patties (GBP), a solid waste generated from cooking fuel used in earthen stoves and Red Soil (RS), a natural substance in fixed bed column mode operation. The characterization of adsorbent was done by Proton Induced X-ray Emission (PIXE), and Proton Induced ${\gamma}$-ray Emission (PIGE) methods. The FTIR spectroscopy of spent adsorbent reveals the presence of absorbance peak at $1127cm^{-1}$ which appears due to P = O stretching, thus confirming phosphate adsorption. The effects of bed height (10, 15 and 20 cm), flow rate (2.5, 5 and 7.5 mL/min) and initial phosphate concentration (5 and 15 mg/L) on breakthrough curves were explored. Both the breakthrough and exhaustion time increased with increase in bed depth, decrease in flow rate and influent concentration. Thomas model, Yoon-Nelson model and Modified Dose Response model were used to fit the column adsorption data using nonlinear regression analysis while Bed Depth Service Time model followed linear regression analysis under different experimental condition to evaluate model parameters that are useful in scale up of the process. The values of correlation coefficient ($R^2$) and the Sum of Square Error (SSE) revealed the Modified Dose Response model as the best fitted model to the experimental data. The adsorbent mixture responded effectively to the desorption and reusability experiment. The results of this finding advocated that mixture of GBP and RS can be used as a low cost, highly efficient adsorbent for phosphate removal from aqueous solution.