Modeling of 2-phenylethanol adsorption onto polymeric resin from aqueous solution: Intraparticle diffusion evaluation and dynamic fixed bed adsorption

被引:13
作者
Cervenansky, Ivan [1 ]
Mihal, Mario [1 ]
Markos, Jozef [1 ]
机构
[1] Slovak Univ Technol Bratislava, Fac Chem & Food Technol, Inst Chem & Environm Engn, Radlinskeho 9, Bratislava 81237, Slovakia
关键词
2-Phenylethanol; Adsorption; Diffusion mechanism; Mathematical modeling; AROMA COMPOUND 2-PHENYLETHANOL; GRANULAR ACTIVATED CARBON; L-PHENYLALANINE; SURFACE-DIFFUSION; BIOTECHNOLOGICAL PRODUCTION; MASS-TRANSPORT; PORE VOLUME; KINETICS; BIOCONVERSION; COEFFICIENTS;
D O I
10.1016/j.cherd.2019.04.042
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Adsorption of 2-phenylethanol from an aqueous solution onto hyper-crossed-linked adsorption resin Macronet MN270 was investigated in a fixed bed column. Adsorption equilibrium was obtained in batch experiments and the results were fitted with the Langmuir isotherm model. A batch adsorption experiment was performed to determine the intraparticle diffusion mechanism. It was found that pore volume diffusion cannot solely govern the intraparticle mass transfer. According to the results of the batch experiment, surface diffusion plays an important role in the adsorption of 2-phenylethanol. Diffusion coefficients obtained in the batch experiment were further verified by comparison of the experimental data with the results of the mathematical model of fixed bed adsorption which was able to predict experimental breakthrough curves obtained under various conditions. A better description of the experimental data was obtained using the mathematical model which considered pore volume diffusion together with surface diffusion. The varying parameters in the measurements of breakthrough curves were: particle diameter, column diameter, volumetric flow rate and the inlet column concentration. Fixed bed adsorption experiments showed that smaller particles together with lower volumetric flow rate produce sharper breakthrough curves. The effect of external mass transfer and axial dispersion was not very significant. Lastly, fixed bed desorption of 2-phenylethanol with water was tested and was shown to be ineffective. Therefore, different solvents for 2-phenylethanol desorption were recommended. (C) 2019 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:292 / 304
页数:13
相关论文
共 34 条
[1]   ADSORPTIVE RECOVERY OF WATER-SOLUBLE ESSENTIAL OIL COMPONENTS [J].
BOHRA, PM ;
VAZE, AS ;
PANGARKAR, VG ;
TASKAR, A .
JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 1994, 60 (01) :97-102
[2]   Adsorption of volatile aroma compound 2-phenylethanol from synthetic solution onto granular activated carbon in batch and continuous modes [J].
Carpine, Danielle ;
Andreotti Dagostin, Joao Luiz ;
da Silva, Vitor Renan ;
Igarashi-Mafra, Luciana ;
Mafra, Marcos Rogerio .
JOURNAL OF FOOD ENGINEERING, 2013, 117 (03) :370-377
[3]   Potential application of perfusion and pertraction for in situ product removal in biocatalytic 2-phenylethanol production [J].
Cervenansky, Ivan ;
Mihal, Mario ;
Markos, Jozef .
SEPARATION AND PURIFICATION TECHNOLOGY, 2017, 183 :11-20
[4]   Production of 2-phenylethanol and 2-phenylethylacetate from L-phenylalanine by coupling whole-cell biocatalysis with organophilic pervaporation [J].
Etschmann, MMW ;
Sell, D ;
Schrader, J .
BIOTECHNOLOGY AND BIOENGINEERING, 2005, 92 (05) :624-634
[5]   Biotechnological production of 2-phenylethanol [J].
Etschmann, MMW ;
Bluemke, W ;
Sell, D ;
Schrader, J .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 2002, 59 (01) :1-8
[6]   FLUID-PARTICLE AND INTRAPARTICLE MASS-TRANSPORT RATES IN SLURRIES [J].
FURUSAWA, T ;
SMITH, JM .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1973, 12 (12) :197-203
[7]   Bioproduction of the Aroma Compound 2-Phenylethanol in a Solid-Liquid Two-Phase Partitioning Bioreactor System by Kluyveromyces marxianus [J].
Gao, Fang ;
Daugulis, Andrew J. .
BIOTECHNOLOGY AND BIOENGINEERING, 2009, 104 (02) :332-339
[8]   Recent advances in biotechnological production of 2-phenylethanol [J].
Hua, Dongliang ;
Xu, Ping .
BIOTECHNOLOGY ADVANCES, 2011, 29 (06) :654-660
[9]   Enhanced 2-phenylethanol production from L-phenylalanine via in situ product adsorption [J].
Hua, Dongliang ;
Lin, Shan ;
Li, Yuanfang ;
Chen, Hong ;
Zhang, Zhaobin ;
Du, Yi ;
Zhang, Xuehong ;
Xu, Ping .
BIOCATALYSIS AND BIOTRANSFORMATION, 2010, 28 (04) :259-266
[10]   Effect of concentration-dependent surface diffusivity on simulation of fixed bed sorption systems [J].
Ko, DCK ;
Porter, JF ;
McKay, G .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2003, 81 (A10) :1323-1332