• Title/Summary/Keyword: multicomponent isotherm

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Pure Gas Adsorption Equilibrium for H2/CO/CO2 and Their Binary Mixture on Zeolite 5A (Zeolite 5A에서의 H2/CO/CO2 단성분 및 혼합성분의 흡착평형)

  • Ahn, Eui-Sub;Jang, Seong-Cheol;Choi, Do-Young;Kim, Sung-Hyun;Choi, Dae-Ki
    • Korean Chemical Engineering Research
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    • v.44 no.5
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    • pp.460-467
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    • 2006
  • Adsorption experiments for $H_2$, $CO_2$, CO, and their binary mixtures on zeolite 5A were performed by static volumetric method. Experimental data were obtained at temperatures of 293.15, 303.15 and 313.15 K and at pressures to 25 atm. The parameters obtained from single component adsorption isotherm. Multicomponent adsorption equilibria could be predicted and compared with experimental data. Langmuir isotherm, Langmuir-Freundlich isotherm and Dual-Site Langmuir isotherm be used to predict the experimental results for binary adsorption equilibria of $CO_2/CO$ and $H_2/CO_2$ on zeolite 5A. Dual-Site Langmuir isotherm showed the best agreement with the experimental results.

Predictive Modeling of Competitive Biosorption Equilibrium Data

  • Chu K.H.;Kim E.Y.
    • Biotechnology and Bioprocess Engineering:BBE
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    • v.11 no.1
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    • pp.67-71
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    • 2006
  • This paper compares regression and neural network modeling approaches to predict competitive biosorption equilibrium data. The regression approach is based on the fitting of modified Langmuir-type isotherm models to experimental data. Neural networks, on the other hand, are non-parametric statistical estimators capable of identifying patterns in data and correlations between input and output. Our results show that the neural network approach outperforms traditional regression-based modeling in correlating and predicting the simultaneous uptake of copper and cadmium by a microbial biosorbent. The neural network is capable of accurately predicting unseen data when provided with limited amounts of data for training. Because neural networks are purely data-driven models, they are more suitable for obtaining accurate predictions than for probing the physical nature of the biosorption process.

Adsorption Characteristics of Heavy Metals in Wastewater on Bone Charcoal (Bone Charcoal에 의한 폐수증의 중금속 흡착특성)

  • Chung, Paul-Gene;Kwak, Dong-Heui;Lee, Jae-Wook
    • Journal of Korean Society on Water Environment
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    • v.16 no.4
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    • pp.555-563
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    • 2000
  • The study was conducted to evaluate the adsorption equilibrium of heavy metals on bone charcoal made of livestock bone which was sintered at $550{\sim}600^{\circ}C$. Analysis of bone charcoal by XRD and FT-IR showed that crystal structure was similar to that of synthetic hydroxyapatite. Adsorption equilibrium capacity of single component (Pb, Cd, and Zn) on bone charcoal could be expressed as Langmuir, Freundlich, and Sips equations. Sips isotherm was best among the three isotherms. The values predicted by IAST(ideal adsorbed solution theory) showed good relationship to the experimental data in multicomponent adsorption equilibrium. Adsorption affinity was in order of Pb, Cd, and Zn. The order was same in case of activated carbon or synthetic hydroxyapatite. Through the study results. it would be expected that bone charcoal made of livestock could be used in field of wastewater treatment plants as adsorbent to remove heavy metal.

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Pure and Binary Gases Adsorption Equilibria of CO2/CO/CH4/H2 on Li-X Zeolite (Li-X 제올라이트에서의 CO2/CO/CH4/H2 단일성분 및 혼합성분의 흡착평형)

  • Park, Ju-Yong;Yang, Se-il;Choi, Do-Young;Jang, Seong-Cheol;Lee, Chang-Ha;Choi, Dae-Ki
    • Korean Chemical Engineering Research
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    • v.46 no.1
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    • pp.175-183
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    • 2008
  • Adsorption equilibria of the gases $CO_2$, CO, $CH_4$ and $H_2$ and their binary mixtures on Li-X zeolite (UOP) were obtained by static volumetric method in the pressure range of 0 to 20 bar at temperatures of 293.15, 303.15, and 313.15 K. Using the parameter obtained from single-component adsorption isotherm. Multicomponent adsorption equilibra could be predicted and compared with experimental data. Extended Langmuir isotherm, Extended Langmuir-Freundlich isotherm (L-F) and dual-site Langmuir isotherm (DSL) were used to predict the experimental results for binary adsorption equilibria of $H_2/CO_2$, $H_2/CO$, and $H_2/CH_4$ on Li-X Zeolite. Extended Langmuir-Freundlich isotherm predicted equilibria of $CH_4$ and $H_2$ better than any other isotherm. One the other hand DSL isotherm predicted equilibria of $CO_2$ and CO very well.

A Study on the Fixed-bed Adsorption of Heavy Metal Ions over Chitosan Bead (키토산 비드에 의한 중금속 이온의 고정층 흡착에 관한 연구)

  • Chung, Kyong-Hwan
    • Applied Chemistry for Engineering
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    • v.10 no.1
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    • pp.166-172
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    • 1999
  • Fixed-bed adsorption of metal ions on chitosan bead was studied to remove heavy metal ions in waste water. Chitin was extracted from carb shell and chitosan was prepared by deacetylation of the chitin. The chitosan in bead was used as an adsorbent for heavy metal ions. Freundlich and Langmuir isotherm was determined from the experimental results of equilibrium adsorption for individual metal ion ($Cu^{2+}$, $Co^{2+}$, $Ni^{2+}$) on chitosan bead. Adsorption strength of metal ions decreased in the order of $Cu^{2+}$>$Co^{2+}$>$Ni^{2+}$ ion. Breakthrough curves of single and multicomponent adsorption for metal ions were obtained from the experimental results of fixed-bed adsorption. The breakthrough curves were analyzed by simulation with fixed-bed adsorption equation based on LDFA (linear driving force approximation) adopted LAS (ideal adsorbed solution) theory which can predict multi-component adsorption isotherm from individual adsorption isotherm. The behavior of fixed bed adsorption for single and multi-component system could be nicely simulated by the equation.

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Effects of activated carbon packing length in PSA process for production of high-purity hydrogen (고순도 수소제조를 위한 PSA 공정에서 활성탄 충전길이 효과)

  • Paik, Eun-gyu;Choi, Min-Ho;Suh, Sung-Sup
    • Clean Technology
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    • v.7 no.2
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    • pp.127-132
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    • 2001
  • The effects of activated-carbon (AC) packing length on the Pressure Swing Adsorption (PSA) performance was investigated for the hydrogen separation from the multicomponent mixture gas. Linear driving force model was used to describe mass transfer between two phase and coupled Langmuir isotherm was used for each component as a nonlinear adsorption isotherm. When two adsorbents with a different adsorption capacity were packed consecutively in one bed, it is very important to determine the packing ratio of zeolite to activated carbon affecting the purity and recovery of the product. The activated carbon packing length in adsorption tower of 120 cm was determinated by the ending point of $CO_2$ contration. The optimum length of an activated carbon layer was 65 cm for production of high-purity hydrogen.

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