A separation membrane, suitably for oil and water separation. The membrane including a porous substrate layer and an active layer arranged over at least a part of the substrate layer. The active layer includes a hydrophilic agent and a superhydrophilic agent. Also described is a method of producing the separation membrane and a drain valve comprising the membrane.

A separation membrane, such as for pressure-assisted oil and water separation. The membrane includes a porous substrate layer and an active layer arranged over at least a part of the substrate layer. The active layer is at least partially crosslinked and comprises a superhydrophilic agent. Also described is a method of producing the separation membrane and a drain valve comprising the membrane.

A method of separating a mixture of fluids may comprise contacting an absorbent material with a mixture of fluids comprising a first fluid and a second fluid having different polarities, wherein the absorbent material selectively absorbs the first fluid to provide a permeate comprising the first fluid and a retentate comprising the second fluid. The absorbent material comprises a zwitterionic polymer, the zwitterionic polymer being a polymerization product of reactants comprising a zwitterionic monomer and a (meth)acrylate crosslinker. The zwitterionic monomer is selected from the group consisting of: a zwitterionic monomer of Formula I, R—(CH.sub.2).sub.m—NR′.sub.2.sup.+—(CH.sub.2).sub.n-A.sup.−, wherein R is selected from a carboxyamide, a (meth)acrylate, and an alkyl; m is an integer of from 0 to 5; each R′ is independently selected from hydrogen and an alkyl; n is an integer of from 1 to 5; and A.sup.− is SO.sub.3.sup.− or CO.sub.2.sup.−; a zwitterionic monomer of Formula II, R—(CH.sub.2).sub.m-A.sup.−-(CH.sub.2).sub.n—NR′.sub.3.sup.+, wherein R is an (meth)acrylate; m is an integer of from 1 to 5; A is PO.sub.4.sup.−; n is an integer of from 1 to 5; and each R′ is independently selected from hydrogen and an alkyl; carboxybetaine diacrylamide; (3-methacryloylamino-propyl)-(2-carboxy-ethyl)-dimethylammonium; 3-[Dimethyl-(2-hydroxyethyl)ammonio]-1-propanesulfonate; 1-methylpyridinium 3-sulfonate; and combinations thereof.

Ion exchange membranes obtainable by curing a composition comprising: (a) a monomer comprising an aromatic group and at least one polymerisable ethylenically unsaturated group; (b) a photoinitiator which has an absorption maximum at a wavelength longer than 380 nm when measured in one or more of the following solvents at a temperature of 23° C.: water, ethanol and toluene; and (c) at least one co-initiator.

A gas separation method is provided. The method includes using a gas separation apparatus comprising a selective permeable membrane and a first and second treatment chambers separated by the selective permeable membrane. A mixed gas containing a gas to be separated is supplied into (or generated within) the first treatment chamber, and the gas to be separated is separated from the mixed gas by having the gas to be separated permeate from the first/second treatment chamber side of the selective permeable membrane, which has a stacked laminated structure of a hydrophilic porous membrane, a separation-functional layer, and a first protective membrane, and the separation-functional layer includes a layer of hydrophilic polymer containing water, and the first treatment chamber is provided on a hydrophilic porous membrane side of the selective permeable membrane and the second treatment chamber is provided on the first protective membrane side of the selective permeable membrane.

The present invention provides a composition for a CO.sub.2 gas separation membrane containing: at least one compound selected from the group consisting of an alkali metal carbonate, an alkali metal bicarbonate, and an alkali metal hydroxide; a crosslinked polymer in which a polymer having a carboxyl group has been crosslinked; and a non-crosslinked polymer obtained by polymerization of one or more monomers selected from the group consisting of vinyl acetate, acrylic acid, methacrylic acid, and a derivative thereof.

Provided are certain membranes useful in the filtration of liquids and removal of various contaminants therein. In certain aspects the membranes have as one component a polyamide such as Nylon 11 and/or Nylon 12. Also provided is methodology for manufacturing such membranes and their use in filtration and purification of liquids. Membranes of the disclosure thus prepared exhibit superior acid stability when compared to polyamide membranes prepared from Nylon 6 or Nylon 6,6.

A gas separation membrane selectively permeable to a specific gas component includes a first porous layer, and a separation function layer provided on a first surface of the first porous layer. The separation function layer contains a hydrophilic resin. The first surface has a wetting tension of greater than or equal to 38 mN/m and less than or equal to 52 mN/m.

One aspect of the present disclosure provides a production method for a porous membrane including pores, and concave portions having an average opening diameter greater than an average pore diameter of the pores on at least one of a pair of main surfaces, the method including a step of forming the concave portion on a surface to be the main surface.

The present invention pertains to separators for electrochemical devices comprising vinylidene fluoride copolymers having improved thermal stability, to a process for their manufacture, and to electrochemical devices comprising the same.