Polymer and Separations Research Laboratory

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08/30/2006

 

Pervaporation

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Organo-Ceramic Composite Pervaporation Membranes for selective Chemical Separations 

 

Recent years have been marked by a growing interest in surface modification of pervaporation membranes by covalent end-attachment of polymer chains. The modification of inorganic membranes for pervaporation applications has been of special interest since the polymer chains alter the surface chemistry of the substrate (i.e., providing selectivity) while the mechanical strength of the membrane is retained. Covalently bonded polymers can be used in good solvent environments since dissolution of the polymer is prevented by its attachment to the substrate. In order to tune the performance of the membrane one has to consider both the chemical and topological properties of the modifying polymer layer.

Past studies have been devoted to the macroscopic properties of the resulting hybrid organic/inorganic materials. However, interest is growing in the nanoscale features which result from the modification process. Since polymers are becoming an important tools in applications such as self-assembled monolayers and micromechanical devices, it is increasingly important to understand and quantify the characteristics of surface-bonded polymers so that surfaces can be engineered for specific applications. Poly(vinyl acetate) was chosen as a model polymer in order to analyze the surface properties resulting from surface modification by a two-step free-radical graft polymerization method. A variety of tools such as atomic force microscopy, thermogravimetric analysis, and scanning electron microscopy were used to examine the dependence of surface features on polymerization reaction conditions such as temperature and monomer concentration. Typical Flory radius of the polymers grafted in the study were found to be 110-170Å, while starting pore sizes of the inorganic membrane substrates used were 50-500Å. It was determined that polymer brush layer of 399Å was able to form on the membrane surface for the specific size and graft density (2.0-3.5 mg/m2 surface) of the polymers produced by the present free radical graft polymerization.

Liquid separation membranes created using the above graft polymerization methods were found to efficiently separate organic mixtures of methanol and methyl-tert-butyl-ether with separation factors up to 100, and aqueous mixtures of TCE and water with separation factors of up to 370. Separation could be increased by increasing the polymer graft yield. Modified membranes displayed remarkably different behavior depending whether the polymer chain size was smaller or larger than the membrane pore size, suggesting that graft polymer size is as important a consideration as polymer chemistry in the modification of porous membrane materials.

 References:

Schematic representation of a laboratory pervaporation system

Separation of Methanol/MTBE Mixtures. Comparison Pervaporation (using nano-structured ceramic-supported polymer membranes) with Isobaric Distillation. Source: Yoshida W., and Y. Cohen (2002).

 

 

 

 

 

 

 

 

 

 

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