The invention provides polymer-grafted and functionalized nonwoven membranes adapted for use in bioseparation processes, the membranes including a nonwoven web of polyester fibers having an average fiber diameter of less than about 1.5 microns, each of the plurality of polyester fibers having grafted thereon a plurality of polymer segments constructed of a methacrylate polymer, each polymer segment carrying a functional group adapted for binding to a target molecule. The invention also provides a method of bioseparation comprising passing a solution comprising the target molecule, such as a protein, through the nonwoven membrane of the invention such that at least a portion of the target molecule in the solution binds to the nonwoven membrane. A method for preparing a polymer-grafted and functionalized nonwoven membrane adapted for use in bioseparation processes is also provided.

Disclosed herein is a gas separation membrane comprising a furan based polymer, an apparatus comprising the gas separation membrane, and a process for separating a mixture of gases using said gas separation membrane. The process comprises contacting one side of a gas separation membrane comprising a furan-based polymer with a mixture of gases having different gas permeances, whereby at least one gas from the mixture of gases permeates preferentially across the gas separation membrane, thereby separating the at least one gas from the mixture of gases.

Disclosed herein is a gas separation membrane comprising a furan based polymer, an apparatus comprising the gas separation membrane, and a process for separating a mixture of gases using said gas separation membrane. The process comprises contacting one side of a gas separation membrane comprising a furan-based polymer with a mixture of gases having different gas permeances, whereby at least one gas from the mixture of gases permeates preferentially across the gas separation membrane, thereby separating the at least one gas from the mixture of gases.

Disclosed herein is a phenolic-graphene oxide composition comprising phenolic-graphene oxide having a carbon to oxygen (C:O) ratio of 2.1 or greater and 5 or less.

After bringing a water-containing peeling liquid in contact with a thin flat film formed on a substrate, a support film including a cover film having one main surface thereof is laminated onto the flat film, such that the support film is in contact with the flat film, a cover film-attached laminate composed of a support film and a cover film is then separated from the substrate, and the laminate including the flat film and the support film is separated from the cover film-attached film.

A filter unit includes an inlet for receiving unfiltered water. A first fluid path directs water through a membrane and a filter element to a first outlet. Additionally, a second fluid path directs water across the membrane and to a second outlet.

A thin film nanocomposite nanofiltration membrane or TFC-NF membrane includes an ultrafiltration support membrane coated with a trimesic acid coating layer. The trimesic acid coating layer is formed or self-assembled on the ultrafiltration support membrane by pouring an aqueous solution of a water soluble tertiary amine on the support membrane to form a first coating layer and then applying a solution of trimesolychloride on the first coating layer. In other words, the trimesic acid coating layer can be formed as a result of the liquid-liquid interface of the water soluble tertiary amine and the trimesolychloride. A total thickness of the TFC-NF membrane can be about 150 ?m. The thin film nanocomposite nanofiltration membrane can be free from MPD monomers.

A thin film nanocomposite nanofiltration membrane or TFC-NF membrane includes an ultrafiltration support membrane coated with a trimesic acid coating layer. The trimesic acid coating layer is formed or self-assembled on the ultrafiltration support membrane by pouring an aqueous solution of a water soluble tertiary amine on the support membrane to form a first coating layer and then applying a solution of trimesolychloride on the first coating layer. In other words, the trimesic acid coating layer can be formed as a result of the liquid-liquid interface of the water soluble tertiary amine and the trimesolychloride. A total thickness of the TFC-NF membrane can be about 150 ?m. The thin film nanocomposite nanofiltration membrane can be free from MPD monomers.

A pressure-resistant porous macromolecular PMMA filter membrane material comprises the following ingredients in parts by weight: 60-95 parts of PMMA, 60-90 parts of MMA, 0.5-25 parts of surfactant and 5-25 parts of water. The filter membrane material is simple in preparation process, and the prepared pressure-resistant porous macromolecular filter membrane material contains no bubble, has a uniform pore size, an adjustable micro pore size of 0.01-12 ?m, a special-purpose pore size of 13-80 ?m, a porosity of 20-38% and a water permeability rate greater than 20%. The filter membrane material has the characteristics of reusability, light weight, high mechanical strength, excellent impact resistance, high pressure resistance, low molding shrinkage, good water permeability, adjustable pore size and the like.

A polymer having a contact angle with water that is greater than or equal to 90? and a contact angle with 1,3-propane diol that is less than 90?. A pervaporation membrane comprising the polymer and a process for purifying a fermentation broth using a pervaporation membrane comprising the polymer is also described.