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Thin film membranes with additives for forward and pressure retarded osmosis

a technology of composite membranes and additives, applied in the direction of membranes, reverse osmosis, coatings, etc., can solve the problems of reducing membrane efficiency and reducing membrane efficiency for fo and pro processes, and achieve the effect of increasing the pressure in the draw solution

Inactive Publication Date: 2009-11-05
FORD GLOBAL TECH LLC +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0008]The increased pressure in the draw solution resulting from transport of the feed solution across the discrimination membrane into the draw solution may be used. Contaminants from the feed solution may be removed resulting from transport of the contaminants across the discrimination membrane into the draw solution.

Problems solved by technology

However, when IFP RO membranes are used for FO or PRO, the solvent, typically water, and the solute, typically water diluted with inorganic or organic salts, or other soluble molecules, tend to dilute each other and reduce membrane efficiency.
Further, the support membrane, which is used primarily for structural support, reduces water flux to some degree, and the solvent and solute become mixed in solution in the thickness of the support membrane structure including a fabric, further reducing membrane efficiency for both FO and PRO processes.

Method used

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  • Thin film membranes with additives for forward and pressure retarded osmosis
  • Thin film membranes with additives for forward and pressure retarded osmosis
  • Thin film membranes with additives for forward and pressure retarded osmosis

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Embodiment Construction

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[0019]Referring now to FIG. 1, an exploded view of membrane 10 illustrating the fabrication process is shown in which membrane 10 may include organic phase layer 18, aqueous phase layer 14, porous support membrane 12 and fabric layer 20. One or more types of nanoparticles 16, or other additives as discussed below in greater detail, may be included in aqueous or organic phases 14, 18 before contact there between for interfacial polymerization so that nanoparticles 16 are dispersed in discrimination layer 24 as shown in FIG. 2. Nanoparticles / additives 16 may also be dispersed in support layer 12 and fabric 20.

[0020]Referring now also to FIG. 2, a portion of membrane 10 is illustrated after fabrication including nanoparticles and / or other additives 16, in discrimination layer 24 as well as nanoparticles / additives 16 in support layer 12 which may be the same or different than those—if any—used in discrimination layer 24. In a conventional thin film composite or TFC membrane, made witho...

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Abstract

A thin film composite or TFC membrane formed by interfacial polymerization of an organic and aqueous phase on a support membrane with nanoparticles in the discrimination layer and / or the support membrane, optimized by the selection of nanoparticles for membrane flux, hydrophilicity and to minimize thickness of the support membrane while maintaining the strength and ruggedness characteristics required for forward osmosis (FO) and / or pressure retarded osmosis (PRO) so that the flux flow paths are less tortuous than conventional support membranes and thereby provide increased flux flow.

Description

CROSS REFERENCE TO RELATED APPLICATIONS[0001]The present application claims the priority of provisional application 61 / 050,572, filed May 5, 2008 and Ser. No.12 / 424,533 filed Apr. 15, 2009, incorporated in herein in full and attached hereto as Appendix A for that purpose.BACKGROUND OF THE INVENTION[0002]1. Field of the Invention[0003]This invention is related to thin film composite membranes, which may be called TFC membranes, and more particularly to such membranes used for forward osmosis or FO, for example to purify water, or for pressure retarded osmosis or PRO, for example to generate power from the mixing of salt water and pure water.[0004]2. Description of the Prior Art[0005]RO membranes are often made by interfacial polymerization or IFP of a monomer in a nonpolar (e.g. organic) phase together with a monomer in a polar (e.g. aqueous) phase on a porous support membrane. The support membrane is used for structural support of the IFP membrane during manufacturing and during ope...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): B01D61/02C02F1/44
CPCB01D61/002B01D61/025B01D63/10B01D67/0079B01D69/125B05D5/00B01D69/148B01D71/56C02F1/445B01D67/0006B01D2325/48B01D69/141Y02A20/131B01D67/00793B01D71/60B01D69/1251B01D67/00791B01D71/82B01D2323/36C02F1/441C02F2103/08
Inventor KURTH, CHRISTOPHER JAMESBURK, ROBERT LEON
Owner FORD GLOBAL TECH LLC
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