A method of making depth filtration media, such as for use in a depth filter, are described. The resulting depth filtration media includes a core tube having two or more different layers. The layers can be fibers, such as polymeric or inorganic fibers, wrapped layers of a filter material, or pleated and folded layers of a filter material.

The invention relates to polymers comprising sulfonated 2,6-diphenyl-1,4-phenylene oxide repeating units, to a method for their preparation, and to their use in a membrane electrode assembly, in a proton exchange membrane, in a fuel cell, in an electrolyser, in an electrolytic hydrogen compressor or in a flow battery. The invention further relates to a proton exchange membrane comprising said polymer and to a method for the preparation of a proton exchange membrane from said polymer. The invention also relates to the use of the polymers in ion exchange materials.

A composite membrane for selectively separating (e.g., pervaporating) a first fluid (e.g., first liquid such as a high octane compound) from a mixture comprising the first fluid (e.g., first liquid such as a high octane compound) and a second fluid (e.g., second liquid such as gasoline). The composite membrane includes a porous substrate comprising opposite first and second major surfaces, and a plurality of pores. A pore-filling polymer is disposed in at least some of the pores so as to form a layer having a thickness within the porous substrate. The composite membrane further includes at least one of: (a) an ionic liquid mixed with the pore-filling polymer; or (b) an amorphous fluorochemical film disposed on the composite membrane.

The present invention relates to modified ceramic membranes for the treatment of water. The invention discloses a modified ceramic membrane, comprising: a ceramic membrane, and an outer surface of said ceramic membrane is grafted by a hydrophilic organosilane, wherein said organosilane is selected from the group consisting of: CH30(C2H40)x(CH2)ySi(OCH3)3, where x is >4 and y is >0; CH30(C2H40)x(CH2)ySi(OCH2CH3)3, where x is >4 and y is>0; (CH30)3Si(CH2)yO(C2H40)x(CH2)ySi(OCH3)3, N where x is >4 and y is >0; and (CH3CH20)3Si(CH2)yO(C2H40)x(CH2)ySi(OCH2CI-13)3, where x is >4 and y is >0.

The object of the present invention is polyphenylene oxide based film with crystalline nanoporous phases with surface area equal to or greater than 30 m2/g, preferably greater than 100 m2/g, and a procedure for the attainment thereof.

A membrane for the capture of carbon dioxide is provided. The membrane includes a polymeric porous hollow fiber substrate and a coating disposed on a surface of the polymeric porous hollow fiber substrate, where the coating comprises graphene oxide and an amine. A method of forming a coated polymeric hollow fiber support for the capture of carbon dioxide is also provided. The method includes dispersing graphene oxide in a coating solution comprising a solvent; dispersing an amine in the coating solution; and exposing a polymeric hollow fiber support to the coating solution to form a coating on a surface of the polymeric hollow fiber support, wherein the coated polymeric hollow fiber support has a carbon dioxide/nitrogen selectivity ranging from about 200 to about 2000 and a carbon dioxide permeance ranging from about 100 gas permeation units to about 1000 gas permeation units.

A membrane for the capture of carbon dioxide is provided. The membrane includes a polymeric porous hollow fiber substrate and a coating disposed on a surface of the polymeric porous hollow fiber substrate, where the coating comprises graphene oxide and an amine. A method of forming a coated polymeric hollow fiber support for the capture of carbon dioxide is also provided. The method includes dispersing graphene oxide in a coating solution comprising a solvent; dispersing an amine in the coating solution; and exposing a polymeric hollow fiber support to the coating solution to form a coating on a surface of the polymeric hollow fiber support, wherein the coated polymeric hollow fiber support has a carbon dioxide/nitrogen selectivity ranging from about 200 to about 2000 and a carbon dioxide permeance ranging from about 100 gas permeation units to about 1000 gas permeation units.

The present invention relates to synthetic membranes and use of these synthetic membranes for isolation of volatile organic compounds and purification of water. The synthetic membrane includes a hydrophobic polymer layer located on a polymeric membrane support layer. The invention includes a method of isolating volatile organic compounds with the synthetic membrane by contacting a volatile organic mixture with the hydrophobic polymer layer of the synthetic membrane and removing volatile organic compounds from the polymeric membrane support layer of the synthetic membrane by a process of pervaporation. The invention also includes a method of purifying water with the synthetic membrane by contacting an ionic solution with the hydrophobic polymer layer of the synthetic membrane and removing water from the polymeric membrane support layer of the synthetic membrane by a process of reverse osmosis. The invention also relates to methods of isolating non-polar gases by gas fractionation.

There is provided a carbon capture mixed matrix membrane comprising: a polymeric support layer; and a carbon dioxide capture layer in contact with the polymeric support layer, the carbon dioxide capture layer comprising solid porous material with at least one carbon dioxide adsorption site, wherein the polymeric support layer comprises spatially ordered uniform sized pores. The polymeric support layer may be patterned by micro-molding, nanoimprinting, mold-based lithography or other suitable lithographic process. The carbon dioxide capture layer may comprise amine-functionalised material, metal-organic frameworks such as zeolite imidazolate framework 8 (ZIF-8) or copper benzene-1,3,5-tricarboxylate (Cu-BTC) which may or may not be amine modified. There is also provided a membrane module comprising at least one carbon capture mixed matrix membrane and a method of forming the carbon capture mixed matrix membrane.

The present application discloses a composite reverse osmosis membrane and a preparation method thereof. The method includes: uniformly mixing fluorine-containing polyaryletherketone of a certain concentration and silane-modified polyaryletherketone as a casting solution; coating a non-woven fabric, i.e., a substrate, with the casting solution to form a support layer; then coating the surface of the support layer with a solution A and a solution B sequentially for reaction to form a polyamide desalination layer; and coating the polyamide desalination layer with a modified polyvinyl alcohol anti-pollution layer. By means of the method, the composite reverse osmosis membrane is prepared. Compared with the prior art, the present application can prepare a composite reverse osmosis membrane with high temperature resistance and high strength by using the composite modified polyaryletherketone as the support layer, and moreover, uses polyvinyl alcohol as a component of the anti-pollution layer, and has good anti-pollution properties.