[[abstract]]The effect of mass transfer in parallel-flow rectangular dialyzers with internal recycle has been investigated. In contrast to the same size device without recycle, considerable improvement in performance is achievable if one of the flow channels, either retentate phase or dialysate phase, is divided into two subchannels of same width (w/2) with one performed as the operating subchannel and the other as the reflux cochannel, which provides the increase in the fluid velocity, resulting in reduction of mass-transfer resistance. The improvement by recycle operation increases both the flow rate of liquid and reflux ratio with negligible amount of hydraulic-dissipated energy.[[booktype]]紙
[[abstract]]The phenomenon of mass transfer through a parallel-plate channel with uniform wall conce...
[[abstract]]The analysis of solvent extraction in the membrane modules of cocurrent, countercurrent ...
[[abstract]]The effect of internal reflux in the raffinate phase for membrane extraction through a c...
[[abstract]]The internal reflux effect on dialysis through the retentate phase of a cross-flow recta...
[[abstract]]The effect of external recycle on the performance of dialysis in countercurrent-flow rec...
100學年度研究獎補助論文[[abstract]]The effect of external recycle on the performance of dialysis in double-pas...
[[abstract]]The predicting equations for mass transfer rate in cross-flow rectangular dialyzers with...
[[abstract]]A study on mass transfer in countercurrent cross-flow rectangular dialyzers with externa...
[[abstract]]Heat transfer in parallel-flow rectangular recuperators with internal recycle has been i...
[[abstract]]Heat transfer in parallel-flow rectangular recuperators with internal recycle has been i...
[[abstract]]The effect of external recycle on the performance of dialysis in cross-flow rectangular ...
[[abstract]]A study on membrane dialysis in parallel-plate rectangular mass exchangers was carried o...
[[abstract]]The analysis of heat transfer in the heat exchangers of cocurrent and countercurrent flo...
[[abstract]]The influence of recycle-barrier location on membrane extraction through a parallel-flow...
[[abstract]]The phenomenon of mass transfer through a parallel-plate channel with uniform wall conce...
[[abstract]]The phenomenon of mass transfer through a parallel-plate channel with uniform wall conce...
[[abstract]]The analysis of solvent extraction in the membrane modules of cocurrent, countercurrent ...
[[abstract]]The effect of internal reflux in the raffinate phase for membrane extraction through a c...
[[abstract]]The internal reflux effect on dialysis through the retentate phase of a cross-flow recta...
[[abstract]]The effect of external recycle on the performance of dialysis in countercurrent-flow rec...
100學年度研究獎補助論文[[abstract]]The effect of external recycle on the performance of dialysis in double-pas...
[[abstract]]The predicting equations for mass transfer rate in cross-flow rectangular dialyzers with...
[[abstract]]A study on mass transfer in countercurrent cross-flow rectangular dialyzers with externa...
[[abstract]]Heat transfer in parallel-flow rectangular recuperators with internal recycle has been i...
[[abstract]]Heat transfer in parallel-flow rectangular recuperators with internal recycle has been i...
[[abstract]]The effect of external recycle on the performance of dialysis in cross-flow rectangular ...
[[abstract]]A study on membrane dialysis in parallel-plate rectangular mass exchangers was carried o...
[[abstract]]The analysis of heat transfer in the heat exchangers of cocurrent and countercurrent flo...
[[abstract]]The influence of recycle-barrier location on membrane extraction through a parallel-flow...
[[abstract]]The phenomenon of mass transfer through a parallel-plate channel with uniform wall conce...
[[abstract]]The phenomenon of mass transfer through a parallel-plate channel with uniform wall conce...
[[abstract]]The analysis of solvent extraction in the membrane modules of cocurrent, countercurrent ...
[[abstract]]The effect of internal reflux in the raffinate phase for membrane extraction through a c...