Embodiments of the present invention relate to a nanofiltration composite membrane for use to purify water, the methods for preparing said nanofiltration composite membranes and to the nanofiltration composite membranes prepared accordingly.

Embodiments of the present invention relate to a nanofiltration composite membrane for use to purify water, the methods for preparing said nanofiltration composite membranes and to the nanofiltration composite membranes prepared accordingly.

The present disclosure relates to synthesis of porous polymer networks and applications of such materials. The present disclosure relates to a method of fabricating of a porous polymer network comprising: (a) providing: (i) a first reactant comprising a plurality of compounds comprising at least one acetyl group, said plurality of compounds comprising at least one compound type, and (ii) a second reactant comprising an alkylsulfonic acid, and (b) creating a solution of said reactants, (c) casting said solution in a form, and (d) treating said solution under such conditions so as to produce a porous polymer network. In one embodiment, the invention relates to a porous polymer network which has a basic structure selected from the group consisting of

##STR00001##

The present disclosure relates to synthesis of porous polymer networks and applications of such materials. The present disclosure relates to a method of fabricating of a porous polymer network comprising: (a) providing: (i) a first reactant comprising a plurality of compounds comprising at least one acetyl group, said plurality of compounds comprising at least one compound type, and (ii) a second reactant comprising an alkylsulfonic acid, and (b) creating a solution of said reactants, (c) casting said solution in a form, and (d) treating said solution under such conditions so as to produce a porous polymer network. In one embodiment, the invention relates to a porous polymer network which has a basic structure selected from the group consisting of

##STR00001##

Provided is a porous membrane that can be manufactured in uncomplicated steps, has high hydrophilicity and water permeability, and exhibits excellent anti-fouling properties when used in a membrane bioreactor method (MBR method). The porous membrane of the present invention is a porous membrane containing polymer (A) and polymer (B), wherein the polymer (A) is a membrane-forming polymer, the polymer (B) is a polymer having a unit (b1) represented by formula (1) and a unit (b2) based on hydroxyl group-containing (meth)acrylate, and the concentration (mass %) of the unit (b1) is equal to or higher than the concentration (mass %) of the unit (b2) in the porous membrane. ##STR00001##

A membrane sorbent is described, which comprises 1-6 wt % silicon carbide nanoparticles dispersed in a polymer matrix. The polymer matrix may comprise polysulfone and polyvinylpyrrolidone. The membrane sorbent is used for separating oil from a contaminated water mixture. The silicon carbide nanoparticles of the membrane sorbent may be made from rice husk ash.

The present disclosure relates to a microporous hollow fiber filter membrane having a large inner diameter and a thin wall. The fiber can be used for sterile filtration of liquids or removal of particles from liquids. The disclosure further relates to a method for producing the membrane and a filter device comprising the membrane.

The present disclosure relates to a microporous hollow fiber filter membrane having a large inner diameter and a thin wall. The fiber can be used for sterile filtration of liquids or removal of particles from liquids. The disclosure further relates to a method for producing the membrane and a filter device comprising the membrane.

A separation membrane module includes a separation membrane including a hydrophobic polymer, a hydrophilic polymer, and polymer A, wherein the polymer A includes a hydrophilic unit and a hydrophobic unit, and is a copolymer having an alkyl group having 2 to 20 carbon atoms at a side-chain terminal of the hydrophobic unit, the separation membrane module having a retention rate of an albumin sieving coefficient of 86% or more at 60 minutes after circulation start relative to an albumin sieving coefficient at 10 minutes after circulation start when 2 L of bovine blood containing 50 U/ml of heparin, and having a hematocrit of 30% by volume and a total protein concentration of 6 to 7 g/dl is circulated at a flow rate of 100 ml/min at 37° C. and a filtration flow rate of 10 ml/(min.Math.m.sup.2).

A separation membrane module includes a separation membrane including a hydrophobic polymer, a hydrophilic polymer, and polymer A, wherein the polymer A includes a hydrophilic unit and a hydrophobic unit, and is a copolymer having an alkyl group having 2 to 20 carbon atoms at a side-chain terminal of the hydrophobic unit, the separation membrane module having a retention rate of an albumin sieving coefficient of 86% or more at 60 minutes after circulation start relative to an albumin sieving coefficient at 10 minutes after circulation start when 2 L of bovine blood containing 50 U/ml of heparin, and having a hematocrit of 30% by volume and a total protein concentration of 6 to 7 g/dl is circulated at a flow rate of 100 ml/min at 37° C. and a filtration flow rate of 10 ml/(min.Math.m.sup.2).