Mathematical modeling and simulation of gel drying with supercritical carbon dioxide
Mathematical models of alumina/silica gel supercritical drying with carbon dioxide were studied using supercritical drying experimental data. An alumina/silica gel with zinc chloride was synthesized and dried with superciritical carbon dioxide, and its weight change wasmonitored as a function of dry...
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Serbian Chemical Society
2005-02-01
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doaj-c0b108ffd0154d09a09bea9f18e8b3312020-11-24T21:29:44ZengSerbian Chemical Society Journal of the Serbian Chemical Society0352-51392005-02-01701125136Mathematical modeling and simulation of gel drying with supercritical carbon dioxideALEKSANDAR ORLOVICSTOJAN PETROVICDEJAN SKALAMathematical models of alumina/silica gel supercritical drying with carbon dioxide were studied using supercritical drying experimental data. An alumina/silica gel with zinc chloride was synthesized and dried with superciritical carbon dioxide, and its weight change wasmonitored as a function of drying time. The pore size distribution of the obtained aerogel was determined using the BET method and nitrogen adsorption/desorption. Themathematical model of the supercritical drying of the wet gel was represented as unsteady and one-dimensional diffusion of solvent through the aerogel pores filled with supercitical carbon dioxide. Parallel pore model and pores in series model were developed on the basis of the measured porous structure of the aerogel. It was found that these models which use different effective diffusivity value for each pore size were in much better agreement with the experimental data than models which use an overall effective diffusivity. The local effective diffusivity coefficients were calculated using different tortuosity values for each pore size, and they were distributed according to the pore size distribution data. Model simulations of the superciritical drying with carbon dioxide confirmed that the drying temperature and gel particle diameter have a significant influence on the drying time.http://www.shd.org.yu/HtDocs/SHD/Vol70/No1/JSCS_V70_No1-14.pdfsupercritical dryingaerogelsmodeling of diffusion |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
ALEKSANDAR ORLOVIC STOJAN PETROVIC DEJAN SKALA |
spellingShingle |
ALEKSANDAR ORLOVIC STOJAN PETROVIC DEJAN SKALA Mathematical modeling and simulation of gel drying with supercritical carbon dioxide Journal of the Serbian Chemical Society supercritical drying aerogels modeling of diffusion |
author_facet |
ALEKSANDAR ORLOVIC STOJAN PETROVIC DEJAN SKALA |
author_sort |
ALEKSANDAR ORLOVIC |
title |
Mathematical modeling and simulation of gel drying with supercritical carbon dioxide |
title_short |
Mathematical modeling and simulation of gel drying with supercritical carbon dioxide |
title_full |
Mathematical modeling and simulation of gel drying with supercritical carbon dioxide |
title_fullStr |
Mathematical modeling and simulation of gel drying with supercritical carbon dioxide |
title_full_unstemmed |
Mathematical modeling and simulation of gel drying with supercritical carbon dioxide |
title_sort |
mathematical modeling and simulation of gel drying with supercritical carbon dioxide |
publisher |
Serbian Chemical Society |
series |
Journal of the Serbian Chemical Society |
issn |
0352-5139 |
publishDate |
2005-02-01 |
description |
Mathematical models of alumina/silica gel supercritical drying with carbon dioxide were studied using supercritical drying experimental data. An alumina/silica gel with zinc chloride was synthesized and dried with superciritical carbon dioxide, and its weight change wasmonitored as a function of drying time. The pore size distribution of the obtained aerogel was determined using the BET method and nitrogen adsorption/desorption. Themathematical model of the supercritical drying of the wet gel was represented as unsteady and one-dimensional diffusion of solvent through the aerogel pores filled with supercitical carbon dioxide. Parallel pore model and pores in series model were developed on the basis of the measured porous structure of the aerogel. It was found that these models which use different effective diffusivity value for each pore size were in much better agreement with the experimental data than models which use an overall effective diffusivity. The local effective diffusivity coefficients were calculated using different tortuosity values for each pore size, and they were distributed according to the pore size distribution data. Model simulations of the superciritical drying with carbon dioxide confirmed that the drying temperature and gel particle diameter have a significant influence on the drying time. |
topic |
supercritical drying aerogels modeling of diffusion |
url |
http://www.shd.org.yu/HtDocs/SHD/Vol70/No1/JSCS_V70_No1-14.pdf |
work_keys_str_mv |
AT aleksandarorlovic mathematicalmodelingandsimulationofgeldryingwithsupercriticalcarbondioxide AT stojanpetrovic mathematicalmodelingandsimulationofgeldryingwithsupercriticalcarbondioxide AT dejanskala mathematicalmodelingandsimulationofgeldryingwithsupercriticalcarbondioxide |
_version_ |
1725965971445776384 |