[[abstract]]Rising fluid velocity in the tubular-membrane module by inserting concentrically a steel rod has two conflicting effects. One, the decrease in resistance to permeation due to reduction in concentration polarization, is good for ultrafiltration, while the other, the decrease in average transmembrane pressure due to increase in friction pressure loss, is bad for ultrafiltration. It appears, therefore, that proper adjustment of fluid velocity as well as proper arrangement of the annular size of flow channel with a specified volumetric feed rate, might effectively suppress any undesirable resistance to permeation while still preserving an effective transmembrane pressure and thereby lead to improved performance of membrane ultrafilt...
The influence of module configuration on the ultrafiltration of highly concentrated fluids in tubula...
One of the processes used in the pulp and paper industry is the ultrafiltration (UF) of fiber suspen...
[[abstract]]Predicting equations for the permeate flux of membrane ultrafiltration in a tubular modu...
[[abstract]]Increasing the fluid velocity in cross-flow membrane ultrafilter has two conflicting eff...
[[abstract]]A hydrodynamic approach developed by a wired-membrane module for reducing the effects of...
[[abstract]]Resistance-in-series analysis of the permeate flux for ultrafiltration in a tubular memb...
[[abstract]]A hydrodynamic approach developed by a wired-membrane module forreducing the effects of ...
[[abstract]]The effect of hydraulic behavior on membrane ultrafiltration in a tubular module inserte...
[[abstract]]Rising fluid velocity in the fiber tubes of a hollow-fiber module has two conflicting ef...
[[abstract]]Predicting equations for the permeate flux of membrane ultrafiltration in a tubular modu...
Predicting equations for the permeate flux of membrane ultra-filtration in a tubular module with a s...
[[abstract]].The permeate flux declination along an ultrafilter membrane is due mainly to the concen...
The major drawback of crossflow membrane filtration is that permeate flux declines with time as a re...
[[abstract]]Predicting equations for the permeate flux of membrane ultrafiltration in wire–rod tubul...
During ultrafiltration (UF), the driving force along the membrane is diminished due to concentration...
The influence of module configuration on the ultrafiltration of highly concentrated fluids in tubula...
One of the processes used in the pulp and paper industry is the ultrafiltration (UF) of fiber suspen...
[[abstract]]Predicting equations for the permeate flux of membrane ultrafiltration in a tubular modu...
[[abstract]]Increasing the fluid velocity in cross-flow membrane ultrafilter has two conflicting eff...
[[abstract]]A hydrodynamic approach developed by a wired-membrane module for reducing the effects of...
[[abstract]]Resistance-in-series analysis of the permeate flux for ultrafiltration in a tubular memb...
[[abstract]]A hydrodynamic approach developed by a wired-membrane module forreducing the effects of ...
[[abstract]]The effect of hydraulic behavior on membrane ultrafiltration in a tubular module inserte...
[[abstract]]Rising fluid velocity in the fiber tubes of a hollow-fiber module has two conflicting ef...
[[abstract]]Predicting equations for the permeate flux of membrane ultrafiltration in a tubular modu...
Predicting equations for the permeate flux of membrane ultra-filtration in a tubular module with a s...
[[abstract]].The permeate flux declination along an ultrafilter membrane is due mainly to the concen...
The major drawback of crossflow membrane filtration is that permeate flux declines with time as a re...
[[abstract]]Predicting equations for the permeate flux of membrane ultrafiltration in wire–rod tubul...
During ultrafiltration (UF), the driving force along the membrane is diminished due to concentration...
The influence of module configuration on the ultrafiltration of highly concentrated fluids in tubula...
One of the processes used in the pulp and paper industry is the ultrafiltration (UF) of fiber suspen...
[[abstract]]Predicting equations for the permeate flux of membrane ultrafiltration in a tubular modu...