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   <subfield code="a">Djekic</subfield>
   <subfield code="D">Tanja</subfield>
   <subfield code="u">Department of Chemical Engineering and Chemistry, Technical University of Eindhoven, Den Dolech 2, Helix, STO 1.27, P.O. Box 513, 5600MB, Eindhoven, Netherlands</subfield>
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   <subfield code="a">Effective intraparticle diffusion coefficients of CoCl2 in mesoporous functionalized silica adsorbents</subfield>
   <subfield code="h">[Elektronische Daten]</subfield>
   <subfield code="c">[Tanja Djekic]</subfield>
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   <subfield code="a">The scope of this work is to determine the effective intraparticle diffusion coefficient of CoCl2 over mesoporous functionalized silica. Silica is selected as a carrier of the functionalized groups for its rigid structure which excludes troublesome swelling, often found in polymeric adsorbents. 2-(2-pyridyl)ethyl-functionalized silica is selected as a promising affinity adsorbent for the reversible adsorption of CoCl2. The adsorption kinetics is investigated with the Zero Length Column (ZLC) method. Initially, experiments were performed at different flow rates to eliminate the effect of external mass transfer. The effect of pore size (60 Å and 90 Å), particle size (40⋅10−6m-1000⋅10−6m) and initial CoCl2 concentration (1 mol/m3-2.0mol/m3) on the mass transfer was investigated. A model was developed to determine the pore diffusion coefficient of CoCl2 by fitting the experimental data to the model. The pore diffusion coefficients determined for two different pore sizes of silica are D p (60 Å) =1.95⋅10−10 [m2/s] and D p (90 Å) =5.8⋅10−10 [m2/s]. The particle size and the initial CoCl2 concentration do not have an influence on the value of diffusion coefficient. However, particle size has an influence on the diffusion time constant. In comparison with polymer adsorbents, silica based adsorbents have higher values of diffusion coefficients, as well as a more uniform and stable pore structure.</subfield>
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   <subfield code="a">Springer Science+Business Media, LLC, 2007</subfield>
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   <subfield code="a">Effective intraparticle diffusion coefficients</subfield>
   <subfield code="2">nationallicence</subfield>
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   <subfield code="a">Mesoporous silica</subfield>
   <subfield code="2">nationallicence</subfield>
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   <subfield code="a">ZLC method</subfield>
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   <subfield code="a">b : Langmuir adsorption constant, m3/mol</subfield>
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   <subfield code="a">C : Adsorbate concentration, mol/ m3</subfield>
   <subfield code="2">nationallicence</subfield>
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   <subfield code="a">C 0 : Initial adsorbate concentration, mol/ m3</subfield>
   <subfield code="2">nationallicence</subfield>
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   <subfield code="a">C e : Equilibrium adsorbate concentration, mol/ m3</subfield>
   <subfield code="2">nationallicence</subfield>
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   <subfield code="a">C NRM : Adsorbate concentration with a non-recycle mode, mol/ m3</subfield>
   <subfield code="2">nationallicence</subfield>
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   <subfield code="a">C RM : Adsorbate concentration with a recycle mode, mol/ m3</subfield>
   <subfield code="2">nationallicence</subfield>
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  <datafield tag="690" ind1=" " ind2="7">
   <subfield code="a">C exp : Experimental adsorbate concentration, mol/ m3</subfield>
   <subfield code="2">nationallicence</subfield>
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  <datafield tag="690" ind1=" " ind2="7">
   <subfield code="a">D a : Macropore diffusion coefficient, m2/s</subfield>
   <subfield code="2">nationallicence</subfield>
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   <subfield code="a">D i : Micropore diffusion coefficient, m2/s</subfield>
   <subfield code="2">nationallicence</subfield>
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   <subfield code="a">D p : Intraparticle diffusion coefficient, m2/s</subfield>
   <subfield code="2">nationallicence</subfield>
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  <datafield tag="690" ind1=" " ind2="7">
   <subfield code="a">F : Volumetric flow, ml/min</subfield>
   <subfield code="2">nationallicence</subfield>
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  <datafield tag="690" ind1=" " ind2="7">
   <subfield code="a">K i : Diffusion time constant, 1/s</subfield>
   <subfield code="2">nationallicence</subfield>
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  <datafield tag="690" ind1=" " ind2="7">
   <subfield code="a">m : Mass of adsorbent, kg</subfield>
   <subfield code="2">nationallicence</subfield>
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  <datafield tag="690" ind1=" " ind2="7">
   <subfield code="a">q : Loading of the adsorbent, mol/kg</subfield>
   <subfield code="2">nationallicence</subfield>
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  <datafield tag="690" ind1=" " ind2="7">
   <subfield code="a">$\bar{q}$ : Averaged loading of the adsorbent, mol/kg</subfield>
   <subfield code="2">nationallicence</subfield>
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  <datafield tag="690" ind1=" " ind2="7">
   <subfield code="a">q exp : Experimentally determined loading of the adsorbent, mol/kg</subfield>
   <subfield code="2">nationallicence</subfield>
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  <datafield tag="690" ind1=" " ind2="7">
   <subfield code="a">q s : Maximal loading of the adsorbent, mol/kg</subfield>
   <subfield code="2">nationallicence</subfield>
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  <datafield tag="690" ind1=" " ind2="7">
   <subfield code="a">r : Radial position in the particle, m</subfield>
   <subfield code="2">nationallicence</subfield>
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   <subfield code="a">R : Radius of the particle, m</subfield>
   <subfield code="2">nationallicence</subfield>
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  <datafield tag="690" ind1=" " ind2="7">
   <subfield code="a">ρ S : Density of the solid, kg/m3</subfield>
   <subfield code="2">nationallicence</subfield>
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  <datafield tag="690" ind1=" " ind2="7">
   <subfield code="a">t : Time, s</subfield>
   <subfield code="2">nationallicence</subfield>
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   <subfield code="a">V : Volume of solution, m3</subfield>
   <subfield code="2">nationallicence</subfield>
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   <subfield code="a">V bed : Volume of the bed in the ZLC set-up, m3</subfield>
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   <subfield code="a">V extra : Volume of the ZLC set-up, m3</subfield>
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   <subfield code="a">V extra * : Volume of the ZLC set-up with empty bed, m3</subfield>
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