Shear stress-based modelling of steady state permeate flux in microfiltration enhanced by two-phase flows [An article from: Chemical Engineering Journal]
Book Details
PublisherElsevier
ISBN / ASINB000RQZ38G
ISBN-13978B000RQZ385
AvailabilityAvailable for download now
Sales Rank99,999,999
MarketplaceUnited States 🇺🇸
Description
This digital document is a journal article from Chemical Engineering Journal, published by Elsevier in 2004. The article is delivered in HTML format and is available in your Amazon.com Media Library immediately after purchase. You can view it with any web browser.
Description:
Crossflow microfiltration experiments without intensification and with two-phase gas-liquid flow were performed on aqueous titanium dioxide dispersions using an alumina tubular membrane. The influence of gas flow velocity on flux was studied. The empirical model for steady state permeate flux and cake thickness prediction was developed. The results of experiments show positive effects of constant gas-liquid two-phase flow on the flux. It was found that there are no operating conditions at which air injection has no effect on the permeate flux. From analysis of the experimental results without gas flow, the empirical model based on Darcy's Law and on mass balance over a membrane module was derived. The model is based on dimensionless numbers regression of all basic operating conditions that influence permeate flux and cake thickness. The results showed good agreement between model prediction and experimental data with gas injection tested on the same apparatus. When the data from a different system (membrane type, membrane material) were taken, the agreement was not so good.
Description:
Crossflow microfiltration experiments without intensification and with two-phase gas-liquid flow were performed on aqueous titanium dioxide dispersions using an alumina tubular membrane. The influence of gas flow velocity on flux was studied. The empirical model for steady state permeate flux and cake thickness prediction was developed. The results of experiments show positive effects of constant gas-liquid two-phase flow on the flux. It was found that there are no operating conditions at which air injection has no effect on the permeate flux. From analysis of the experimental results without gas flow, the empirical model based on Darcy's Law and on mass balance over a membrane module was derived. The model is based on dimensionless numbers regression of all basic operating conditions that influence permeate flux and cake thickness. The results showed good agreement between model prediction and experimental data with gas injection tested on the same apparatus. When the data from a different system (membrane type, membrane material) were taken, the agreement was not so good.
