• 제목/요약/키워드: freundlich model

검색결과 306건 처리시간 0.025초

가스 및 유기용제용 호흡보호구의 정화통에 대한 수명예측방법의 정확도 및 타당성 검증연구 (Study on Accuracy and Validity Tests for Various Prediction Models for Gas and Vapor Respirator Cartridge Service Lives)

  • 박두용;박지영;윤충식
    • 한국산업보건학회지
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    • 제9권2호
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    • pp.19-31
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    • 1999
  • Most breakthrough tests are conducted at higher concentration levels compared to those in the field of air-purifying respirator applications. For example, typical challenge concentrations for breakthrough tests agains tcarbon tetrachloride are ranged between 250-1000 ppm although applicable concentrations range for air-purifying cartridge is 5-50 ppm for carbon tetrachloride. However, no guarantee has been made that isotherms derived from the experiment at high challenge concentrations could estimate adsorption capacity at the lower concentration range where workers wear usually air-purifying respirators. Three models of adsorption isotherms (Freundlich, Langmuir and Dubinin/Radushkevich(D/R) isotherms) that have been commonly applied for respirator cartridge testing were evaluated. Adsorption capacity at each challenge concentration was calculated from the Reaction Kinetic equation fitted for the breakthrough data. These data were used for derivation of three isotherms. In general, the D/R isotherm has given the best agreement between estimated adsorption capacities and experimentally measured. If the challenge concentration of 100 ppm is included for derivation of models, Freundlich and D/R models could succes sfully produced good estimations for adsorption capacities at 50 ppm level. Estimated adsorption capacities by both models ranged in 94 - 109 % of the experimentally measured. However, Langmuir model gives underes timation in all cases.

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반응표면분석법을 이용한 Hydroxyapatite 첨가 활성탄에서의 Cd 흡착특성에 관한 연구 (Adsorption Characterization of Cd by Activated Carbon containing Hydroxyapatite using Response Surface Methodology (RSM))

  • 안상우;유지영;최재영;박재우
    • 한국물환경학회지
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    • 제25권6호
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    • pp.943-950
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    • 2009
  • Cadmium (Cd) adsorption onto the activated carbon containing hydroxyapatite (HAP) was investigated in batch experiments and response surface methodology (RSM) using the Box-Behnken methods were applied to the experimental results. Cd adsorption with different HAP mass ratio of from 10% to 30%. With more HAP, Cd was more adsorbed. These results suggest that the higher HAP mass causes an increase of the ion exchange potential of the HAP sorbent. Equilibrium experimental results from Cd adsorption was fitted to Langmuir and Freundlich isotherm models. Cd adsorption on HAP sorbent were found to follow the Freundlich isotherm model well in the initial adsorbate concentration range. Also, Cd adsorption was a function of the HAP mass ratio ($x_1$), initial Cd concentration ($x_2$), and initial pH ($x_3$) from the application of the RSM. Statistical results showed the order of significance of the independent variables to be initial Cd concentration > HAP mass ratio > initial pH.

비선형과 선형 등온흡착식을 이용한 키토산비드의 구리와 인산염의 흡착특성 (Adsorption characteristic of Cu(II) and phosphate using non-linear and linear isotherm equation for chitosan bead)

  • 김태훈;안병렬
    • 상하수도학회지
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    • 제34권3호
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    • pp.201-210
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    • 2020
  • 2 (Langmuir, Freundlich, Elovich, Temkin, and Dubinin-Radushkevich) and 3 (Sips and Redlich-Peterson)-parameter isotherm models were applied to evaluated for the applicability of adsorption of Cu(II) and/or phosphate isotherm using chitosan bead. Non-linear and linear isotherm adsorption were also compared on each parameter with coefficient of determination (R2). Among 2-parameter isotherms, non-linear Langmuir and Freundlich isotherm showed relatively higher R2 and appropriate maximum uptake (qm) than other isotherm equation although linear Dubinin-Radushkevich obtained highest R2. 3-parameter isotherm model demonstrated more reasonable and accuracy results than 2-parmeter isotherm in both non-linear and linear due to the addition of one parameter. The linearization for all of isotherm equation did not increase the applicability of adsorption models when error experiment data was included.

실로퓨트에 의한 아세나프텐 흡착에 관한 등온흡착식, 동역학 및 열역학적 특성 (Isotherm, Kinetic and Thermodynamic Characteristics for Adsorption of Acenaphthene onto Sylopute)

  • 조다님;김진현
    • Korean Chemical Engineering Research
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    • 제58권1호
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    • pp.127-134
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    • 2020
  • 상용흡착제 실로퓨트에 의한 Taxus chinensis 유래 주요 타르 성분인 아세나프텐의 흡착 특성을 조사하였다. 초기 아세나프텐 농도, 흡착 온도 및 시간에 따른 흡착 데이터를 Langmuir, Freundlich, Temkin 및 Dubinin-Radushkevich 등온흡착식에 적용한 결과, Langmuir 등온흡착식이 가장 적합하였다. 동역학적 흡착 데이터는 유사 이차 속도식에 가장 잘 따름을 알 수 있었다. 열역학적 파라미터로부터 흡착 공정이 적합하며 비자발적 발열이었다. 등량흡착열은 흡착량에 의존하지 않아 실로퓨트의 표면에너지가 균일함을 알 수 있었다.

Sorption Isotherms and KocS Estimation of Pyrethroids in Sediments

  • Lee, Sang-Jin;Shin, Hyun-Moo
    • 한국환경과학회지
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    • 제12권11호
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    • pp.1173-1179
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    • 2003
  • Laboratory sorption isotherm batch studies have been attempted to elucidate interaction of synthetic pyrethroids (bifenthrin and permethrin) with sediments and their fractions. As a nonlinear isothermal model, the Freundlich equation was applied to sorption results obtained from sediments to investigate the relationship between synthetic pyrethroids and sediments containing different amounts of organic carbon. Results demonstrated that the sorption capabilities of bifenthrin and cis- and trans-permethrin was in the order of bifenthrin, cis-permethrin and trans-permethrin, respectively, indicating that adsorbed bifenthrin was the most stable followed by cis- and trans-permethrin in all sediments. Their sorption capability was closely related to organic carbon contents in sediments. Higher sorption was observed in sediments containing higher organic carbon contents. Sorption study extended into the fractions, clay and humic acids, extracted from a sediment, indicated that higher sorption capacity in humic acids occurred than in the clay of both examined bifenthrin and permethrin. This study demonstrates the sorption of synthetic pyrethroids with sediments, and will help in the understanding of the transport and fate of synthetic pyrethroids existing in field sediments.

양극산화 공정을 이용한 Iron Oxide Nanotubes의 제조 및 수중 인 흡착 (Fabrication of Iron Oxide Nanotubes by Anodization for Phosphorus Adsorption in Water)

  • 이원희;임한수;김종오
    • 상하수도학회지
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    • 제30권6호
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    • pp.691-698
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    • 2016
  • This study was carried out to investigate the characterization of iron oxide nanotubes (INTs) by anodization method and applied adsorption isotherms and kinetic models for phosphate adsorption. SEM analysis was conducted to examine the INTs surface formation. Further XRD and XPS analysis were performed to observe the crystal structure of INTs before and after phosphate adsorption. AFM analysis was conducted to determine of Fe foil surface before and after anodization. Phosphate stock solution for adsorption experiment was prepared by $KH_2PO_4$. The batch experiment was conducted using 20 ml phosphate stock solution and $40cm^3$ of INTs in 50 ml conical tube. Adsorption isotherms were applied Langmuir and Freundlich models for adsorption equilibrium test of INTs. Pseudo first order and pseudo second order models were applied for interpretation of adsorption rate by reaction time. The determination coefficient ($R^2$) values of Langmuir and Freundlich models were 0.9157 and 0.8876 respectively.

활성탄에 흡착된 페놀의 아세톤 탈착 모델에 대한 연구 (Mathematical Modelling of Phenol Desorption from Spent Activated Carbon by Acetone)

  • 김승도;오영진
    • 대한환경공학회지
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    • 제22권12호
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    • pp.2115-2123
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    • 2000
  • 본 연구는 활성탄 피흡착물인 페놀의 아세톤에 의한 탈착모델 및 탈착 동역학을 결정하여 활성탄으로부터 페놀이 탈착되는 현상을 구명하는데 그 목적을 두고 있다. 아세톤에 의한 페놀의 Freundlich 등온탈착 평형반응상수인 $k_e$는 온도의 함수로서 다음과 같이 표현된다: $k_e(T)=0.1{\cdot}exp(797.297/T)$. 또한 Freundlich 등온탈착 평형반응상수인 n은 약한 온도함수로서 $50^{\circ}C$ 이하에서는 용도에 따라 큰 영향을 받지 않으나, $100^{\circ}C$ 이상에서는 5% 이상 차이가 나기 때문에 온도에 대한 보정치를 적용하는 것이 필요하다. 페놀 탈착모델은 활성탄 표면에서의 탈착반응을 제한반응으로 가정하였으며, 탈착반응상수 ($k_d$)는 실험치와 모델 이론치의 최적합도에서 결정하였고, Arrhenius 관계식으로 다음과 같이 표현된다: $k_d( sec^{-1})=0.0479{\cdot}exp(-3037/T)$. 모델에서 결정한 $k_d$값을 검증하기 위해 다른 반응조건에서의 실험결과와 이론치를 비교하였으며, 두 값의 차이가 5% 이내인 것을 미루어 본 연구에서 설정한 탈착반응모델이 타당한 것으로 추정된다. 본 모델을 이용한다면 특정조건(온도, 용매 부피, 활성탄 양, 페놀 초기 흡착량)에서의 재생시간과 재생율을 결정할 수 있으며, 본 실험에서 사용한 조건에 근거한 재생시간과 재생율을 온도의 함수로서 표현할 수 있다: (1) 재생시간 : ${\tau}_{reg}(hr)=-0.08130T_c+8.4775$, (2)재생율 : ${\eta}(%)=0.2210T_c+83.745$. 이 식을 적용하는 경우 반응온도 15, 55, $100^{\circ}C$에서 재생시간은 각각 7, 4.2, 0.35시간. 한편 재생율은 87, 96, 99%로 결정할 수 있다.

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탄화분변토를 이용한 Benzene의 흡착특성 (Adsorption Characteristics of Benzene by Carbonized Cast)

  • 김재홍;손희정;김미룡
    • 환경위생공학
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    • 제14권1호
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    • pp.97-102
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    • 1999
  • This study was carried out view that reuse of sludge of adsorbent for benzene in carbonized cast compare with activated carbon. Not only the carbonized cast is good than carbonized carbon in cation exchange capacity and 12 adsorption capacity, but also benzene adsorption capacity is no differences compare to activated carbon. As results, benzene adsorption capacity of carbonized cast and activated carbon are decreased as temperature increase($25~70^{\circ}C$).It is compatible in Lamgmuir model. Therefore, carbonized cast is applied general adsorbent. From experimental results and data regression, in model concerning effect of temperature, relative errors between the experimental data and those calculated by the model are within the range of 1.2~7.8%. In relative humidity effect (RH 0.25~0.50) of benzene adsorption, modified Freundlich model : $QB_{enzene}{;\}QB_{enzene},{\}_{RH=0}=1-kRH^{IN}$, relative errors between the experimental data and those calculated by the model are within are range of 0.5-5.1%. The constants k and l/n in equation were found to be 1.25, 1.89 in carbonized cast.

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Saccharomyces cerevisiae와 Aureobasidium pullulans의 수은제거 모델 (Biosorption Model of Mercury by Saccharomyces Cerevisiae and Aureobasidium Pullulans)

  • 서정호;서명교;강신묵;이국의;최윤찬;조정구;김의용
    • 한국환경보건학회지
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    • 제23권4호
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    • pp.21-25
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    • 1997
  • A study on the removal of mercury by Saccharomyces cerevisiae and Aureobasidium pullulans was done, in which the model of adsorption isotherm and adsorption rate was proposed. The adsorption isotherm of mercury by S. cerevisiae was accorded with Langmuir model but A. pullulans was followed to Freundlich model. The amount of mercury removed by A. pullulans was higher than that of S. cerevisiae, but the adsorption rate of mercury by A. pullulans was slower than that of S. cerevisiae. In a rapid adsorption process, therefore, it is more useful to use S. cerevisiae as a biosobent.

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활성탄에 의한 Reactive Orange 16 염료 흡착에 대한 공정 파라미터 연구 (Study on of Process Parameters for Adsorption of Reactive Orange 16 Dye by Activated Carbon)

  • 이종집
    • 한국산학기술학회논문지
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    • 제21권7호
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    • pp.667-674
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    • 2020
  • 활성탄에 의한 reactive orange 16 (RO 16) 염료의 흡착은 흡착제의 양, pH, 초기 농도, 접촉시간과 온도를 흡착변수로 사용하여 실험하였으며, 분리계수, 속도상수, 율속단계, 활성화 에너지, 엔탈피, 엔트로피, 자유에너지와 같은 공정 파라미터에 대해 조사하였다. RO 16의 흡착은 활성탄 표면의 양이온 (H+)과 RO 16이 가지고 있는 설포네이트 이온 및 수산 이온사이의 정전기적 인력으로 인해 pH 3에서 흡착율이 가장 높았다. 등온자료는 Langmuir, Freundlich 및 Temkin 등온식을 적용하였다. Freundlich 상수(1/n=0.398~0.441)와 Langmuir 분리계수(RL=0.459~0.491)에 의해 활성탄에 의한 RO 16의 흡착조작은 적절한 제거방법임을 확인하였다. Temkin 식의 흡착에너지 (BT=0.293~0.576 kJ/mol) 값으로부터 이 흡착공정이 물리흡착공정이라는 것을 알았다. 흡착 동력학 실험은 RO 16의 흡착이 유사이차반응속도식에 잘 맞는 것으로 나타났다. 흡착공정의 율속단계는 입자 내 확산 단계인 것이 확인되었다. 양수값의 엔탈피 변화는 물리흡착임을 나타냈다. 음수값의 깁스 자유에너지 변화는 온도가 올라갈수록 -3.16<-11.60<-14.01 kJ/mol 순으로 작아졌다. 따라서 RO 16의 흡착공정의 자발성이 온도가 증가할수록 높아진다는 것을 보여주었다.