An article that can be used for biomaterial capture comprises (a) a porous substrate; and (b) borne on the porous substrate, a polymer comprising interpolymerized units of at least one monomer consisting of (1) at least one monovalent ethylenically unsaturated group, (2) at least one monovalent ligand functional group selected from acidic groups, basic groups other than guanidino, and salts thereof, and (3) a multivalent spacer group that is directly bonded to the monovalent groups so as to link at least one ethylenically unsaturated group and at least one ligand functional group by a chain of at least six catenated atoms.

An article that can be used for biomaterial capture comprises (a) a porous substrate; and (b) borne on the porous substrate, a polymer comprising interpolymerized units of at least one monomer consisting of (1) at least one monovalent ethylenically unsaturated group, (2) at least one monovalent ligand functional group selected from acidic groups, basic groups other than guanidino, and salts thereof, and (3) a multivalent spacer group that is directly bonded to the monovalent groups so as to link at least one ethylenically unsaturated group and at least one ligand functional group by a chain of at least six catenated atoms.

A three-dimensionally ordered macroporous hydrogel for immobilizing a selected bioresponsive molecule and method of making are disclosed. The three-dimensionally ordered macroporous hydrogel comprises a crosslinked polymer that has a system of interconnected pores. The interconnected pores have a uniform pore size in the range of 50 to 5000 nm, and a plurality of first pore functional groups. The plurality of first pore functional groups is selected to immobilize a selected bioresponsive molecule. Examples of bioresponsive molecules include an enzyme; a molecule for: a protein scaffold, solid phase synthesis, nucleic acid synthesis, polypeptide synthesis, analyte detection, adsorption of analytes and measuring analyte concentrations, organic synthesis, and degradation of biologically active agents in wastewater. A method includes forming a colloidal crystal template, polymerizing a hydrogel within the pores of the colloidal crystal template, and selectively removing the colloidal crystal template. The hydrogel can be polymerized using CRP, ATRP and FRP polymerization processes.

The present disclosure provides a high-temperature-resistant deep penetration molecular membrane acid copolymer and a preparation method thereof. The copolymer is formed by polymerizing four raw monomers including 2-acrylamido-2-methylpropanesulphonic acid, vinyl phosphonic acid, alkyl dimethylallyl ammonium chloride, and perfluoropolyether acrylate. The method comprises: S1: mixing and stirring solvent oil, an emulsifier, the alkyl dimethyl allyl ammonium chloride, and the perfluoropolyether acrylate to be dispersed homogeneously to obtain an oil phase; S2: mixing and stirring the 2-acrylamido-2-methylpropanesulphonic acid, the vinyl phosphonic acid, a complexing agent, and distilled water, and adjusting pH to obtain an aqueous phase; S3: slowly dropwise adding the aqueous phase to the oil phase; and S4: introducing nitrogen into the water-in-oil emulsion to remove oxygen, then adding an initiator and carrying out a heating polymerization reaction to obtain copolymer emulsion (i.e., a molecular membrane agent). The copolymer emulsion is added to an acid solution to obtain molecular membrane acid.

A water-treatment separation membrane with good antifouling properties includes a support having pores, a polyamide layer formed on the support, and a passivation layer comprising specific materials formed on the polyamide layer.

Membranes, methods of making the membranes, and methods of using the membranes are described herein. The membrane can include a support layer; and a selective polymer layer disposed on the support layer. The selective polymer layer can include a selective polymer matrix that comprises a mobile carrier comprising an alkanolamine or a salt thereof. The selective polymer matrix can further comprise, for example, a hydrophilic polymer, a cross-linking agent, a low molecular weight amino compound, an amine-containing polymer, a CO.sub.2-philic ether, or a combination thereof. In some embodiments, the selective polymer matrix can further comprise graphene oxide dispersed within the selective polymer matrix. The membranes can be used to separate carbon dioxide from hydrogen. Also provided are methods of purifying syngas using the membranes described herein.

The invention relates to a method for assembling a bipolar membrane, and bipolar membrane thereof. The method comprises the steps of electrospinning and centrifugal spinning and electrocentrifugal spinning a first cation exchange layer comprising a first water splitting catalyst and a first cation exchange polymer, electrospinning and centrifugal spinning and electrocentrifugal spinning a junction layer. Further, the method comprises electrospinning and centrifugal spinning and electrocentrifugal spinning a first anion exchange layer comprising a second water splitting catalyst and a first anion exchange polymer. A system comprising a bipolar membrane according to the invention is also disclosed.

The present disclosure provides an article including an isoporous membrane disposed on a porous substrate. The isoporous membrane includes a triblock copolymer or a pentablock copolymer. The isoporous membrane has a thickness and is isoporous throughout its thickness. A method of making an article is also provided, which does not require a solvent exchange process. The method includes depositing a composition on a porous substrate, thereby forming a fdm, and removing at least a portion of the solvent from the film, thereby forming an isoporous membrane having numerous pores. The composition contains a solvent and solids including a triblock copolymer or a pentablock copolymer. The article advantageously can be hydrophilic and provides sharp molecular weight cut-offs and high flux.

A polyether compound having a cationic group and two or more chain end groups and, wherein all of the chain end groups are any of a hydroxyl group and an azide group is provided.

Provided is a composite semipermeable membrane including: a support membrane; a separation functional layer containing a crosslinked polyamide disposed on the support membrane; and a coating layer disposed on the separation functional layer, in which a developed area ratio Sdr of a coating layer-side surface of the composite semipermeable membrane is 60% to 200%, and a static friction coefficient us between the coating layer-side surface of the composite semipermeable membrane and a lapping film abrasive having a particle size of #2000 is 0.40 to 1.30.