Mesoporous Poly (Aryl Ether Ketone) Hollow Fiber Membranes And Use Thereof In Mass Transfer Processes

Abstract

A process for the efficient transfer of molecules between phases employing mesoporous poly (aryl ether ketone) hollow fiber membranes is provided. The method addresses the controlled transfer of reactants into and removal of reaction products from a reaction media and the removal and separation of target molecules from process streams by membrane-assisted liquid-liquid extraction. A number of possible modes of liquid-liquid extraction are possible according to the invention by utilizing porous poly (aryl ether ketone) hollow fiber membranes of Janus-like structure that exhibit a combination of hydrophilic and hydrophobic surface characteristics. The method of the present invention can address the continuous manufacture of chemicals in membrane reactors and is useful for a broad range of separation applications, including separation and recovery of active pharmaceutical ingredients.

1 . A membrane reactor configured for transferring at least one molecule from a first fluid phase into a second fluid phase across an asymmetric porous hollow fiber membrane by contacting a first side of the asymmetric porous hollow fiber membrane with the first phase containing the at least one molecule dissolved in the first phase, contacting a second side of the asymmetric porous hollow fiber membrane with the second phase so that the first phase and the second phase come into contact through pores of the asymmetric porous hollow fiber membrane, and removing the first phase depleted of the at least one dissolved molecule from the first side of the asymmetric porous hollow fiber membrane while removing the second phase enriched with the at least one dissolved molecule from the second side of the asymmetric porous hollow fiber membrane, wherein the asymmetric porous hollow fiber membrane is formed by a multi-step process comprising the steps of:
 (a) forming a blend of a poly (aryl ether ketone) polymer with a polyimide;   (b) forming a hollow fiber shaped article from the blend by melt processing, wherein the article is substantially amorphous;   (c) subjecting a surface of the article to a solvent treatment step that induces crystallization in the article to a predetermined depth;   (d) subjecting the article, subsequent to step (c), to a second crystallization step to complete crystallization;   (e) bringing the article into contact with a solution of primary amine or hydrazine to affect decomposition of the polyimide; and   (f) removing products of polyimide decomposition from the article.   
     
     
         2 . The membrane reactor of  claim 1  wherein the at least one molecule is a reactant transferred from the first phase into the second phase. 
     
     
         3 . The membrane reactor of  claim 1  wherein the at least one molecule is a reaction product removed from the first phase into the second phase. 
     
     
         4 . The membrane reactor of  claim 1  wherein functional groups are introduced on the surface of the article prior to step (e). 
     
     
         5 . The membrane reactor of  claim 4  wherein the functional groups on the surface of the article are introduced via reaction with benzophenone segments of a polymeric backbone of the poly(aryl ether ketone) polymer. 
     
     
         6 . The membrane reactor of  claim 5  wherein the functional groups on the surface of the article are reacted with functional organic molecules to form a separation layer covalently attached to the surface of the article via the functional groups. 
     
     
         7 . The membrane reactor of  claim 4  wherein the functional groups are selected from: primary, secondary, tertiary or quaternary amine groups, a carboxyl group, a sulfonic acid group, a phosphate group, primary, secondary or tertiary hydroxyl groups, an ethylene oxide group and/or a sulfhydryl group. 
     
     
         8 . The membrane reactor of  claim 1  wherein no transfer of the first phase into the second phase takes place under conditions that a pressure differential existed between the phases 
     
     
         9 . The membrane reactor of  claim 1  wherein the first phase is a gas and the second phase is a liquid. 
     
     
         10 . The membrane reactor of  claim 1  wherein the crystallization in step (c) is carried out in an alcohol, a ketone, a chlorinated hydrocarbon, polyethylene glycol, an aromatic hydrocarbon or a mixture thereof. 
     
     
         11 . The membrane reactor of  claim 11  wherein the ketone is an acetone, a methyl ethyl ketone, a 2-hexanone, an isophorone, a methyl isobutyl ketone, a cyclopentanone, an acetophenone, a valerophenone, a pentanone or a mixture thereof or a mixture with water. 
     
     
         12 . The membrane reactor of  claim 1  wherein the crystallization to the predefined depth in step (c) defines a surface layer that is mesoporous. 
     
     
         13 . The membrane reactor of  claim 12  wherein a thickness of the mesoporous surface layer is less than 1 micron. 
     
     
         14 . The membrane reactor of  claim 1  wherein the poly (aryl ether ketone) comprises a poly (ether ketone), a poly (ether ether ketone), a poly (ether ketone ketone), a poly (ether ether ketone ketone) or a poly (ether ketone ether ketone ketone). 
     
     
         15 . The membrane reactor of  claim 1  wherein the polyimide is a mixture of polyimides or a mixture of a polyimide with an additional pore-forming material. 
     
     
         16 . The membrane reactor of  claim 1  wherein the polyimide is a poly (ether imide). 
     
     
         17 . The membrane reactor of  claim 12  wherein the mesoporous surface layer exhibits an average pore diameter smaller by at least factor of two than an average pore diameter of an interior of the article. 
     
     
         18 . The membrane reactor of  claim 17  wherein the average pore diameter of the surface layer is less than 70 nm. 
     
     
         19 . The membrane reactor of  claim 12  wherein the mesoporous surface layer exhibits an average pore diameter falling within the range of 5 nm to 20 nm. 
     
     
         20 . The membrane reactor of  claim 1  wherein the asymmetric porous hollow fiber membrane has a pore volume between 40 and 80%. 
     
     
         21 . The membrane reactor of  claim 1  wherein the asymmetric porous hollow fiber membrane exhibits a degree of crystallinity of at least 20%. 
     
     
         22 . The membrane reactor of  claim 1  wherein the crystallization in step (d) is carried out by a thermal treatment at a temperature between 210° C. and 310° C. 
     
     
         23 . The membrane reactor of  claim 4  wherein the functional groups are formed by reduction of ketone groups in a benzophenone segment of the polymeric backbone to hydroxyl groups. 
     
     
         24 . The membrane reactor of  claim 23  wherein the ketone group reduction is carried out utilizing sodium borohydride solution in an alcohol/water solvent mixture, or an alcohol/polyethylene glycol solvent mixture or a tetrahydrofuran/polyethylene glycol solvent mixture. 
     
     
         25 . The membrane reactor of  claim 23  wherein the hydroxyl groups are further reacted with functional epoxide molecules.