شماره ركورد كنفرانس :
5048
عنوان مقاله :
AN IMPROVMENT IN ADSORPTION-TRANSPORTMODEL FOR ANIONS TRANSMISSION THROUGH NANOFILTRATIONMEMBERANE: A NEWPOROSITY MODEL
Author/Authors :
S. S ،Madaeni Chemical Engineering Department - Razi University Kermanshah, Iran , E ،Salehi Chemical Engineering Department - Razi University Kermanshah, Iran
كليدواژه :
Modeling , membrane , adsorption-transport , porosity , screen phenomenon
عنوان كنفرانس :
ششمين كنگره بين المللي مهندسي شيمي
چكيده لاتين :
In a previous work published by the current authors, a mathematical model for transport and adsorption of
saturated brine-anions through negatively charged nanofiltration membrane was introduced. This model was a
combination of convection-diffusion equation in unsteady form with adsorption isotherms. In this study the proposed
model was improved using a new adsorption- based porosity model. A novel dynamic model was derived for bulk
porosity estimation on the basis of the adsorption rate and accumulation of anions on the membrane matrix during
filtration process. Finally, the anion's transport partial differential equations and obtained bulk porosity relationship
were combined and solved simultaneously. Introducing the variation of bulk porosity along the filtration process, results
in a slight improvement in recent model predictions.