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Experimental investigation on a membrane distillation based micro-separator
Authors:Chafika Adiche  Kai Sundmacher
Affiliation:1. Otto-von-Guericke-University Magdeburg, Process Systems Engineering, Sandtorstrasse 1, D-39106 Magdeburg, Germany;2. Max-Planck Institute for Dynamics of Complex Technical Systems, Sandtorstrasse 1, D-39106 Magdeburg, Germany
Abstract:In this work a novel micro-separator combining the sweep gas membrane distillation principle with micro-fluidic channels was designed and tested for the separation of a mixture of methanol and water with a low to high methanol concentration. The performance of the new separation device was studied with different liquid–vapor/gas membrane contactors with respect to the separation factor and the distillate flux rate by varying the relevant operating parameters of the process like the methanol concentration in the feed (5–70 wt.%), the feed temperature (40–65 °C), the feed flow rate (up to 30 ml/min), and the flow rate of the inert carrier gas nitrogen (up to 600 ml/min at standard conditions). For all performed experiments, the feasibility of the separation has been proved and the possibility to separate mixtures with high methanol concentration by using a membrane distillation based micro-separator has been for the first time reported. The inert gas flow rate was identified as the crucial operating parameter influencing the separation performance of the micro-separator. In addition, the selection of an appropriate membrane liquid–vapor/gas contactor was found to be an important design parameter for the reduction of temperature polarization effects.
Keywords:Micro-separation  Sweep gas membrane distillation  Micro-fluidic structure  Liquid&ndash  vapor/gas membrane contactor  Aqueous mixture with high methanol concentration  Process intensification  Miniaturization
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