A porous membrane has a thickness of 150 m or greater. The pore diameters of a first surface are smaller than the pore diameters of a second surface. The average value of the pore diameters of the first surface is 60 nm or less, and the coefficient of variation of the pore diameters is 10% or greater and 50% or less.

A porous membrane has a thickness of 150 m or greater. The pore diameters of a first surface are smaller than the pore diameters of a second surface. The average value of the pore diameters of the first surface is 60 nm or less, and the coefficient of variation of the pore diameters is 10% or greater and 50% or less.

The present disclosure provides cassettes for use in automated cell engineering systems that include cell concentration filters for reducing fluid volume of a cell sample during or following automated processing. The disclosure also provides methods of concentrating a cell population, as well as automated cell engineering systems that can utilize the cassettes and carry out the methods.

The present disclosure provides cassettes for use in automated cell engineering systems that include cell concentration filters for reducing fluid volume of a cell sample during or following automated processing. The disclosure also provides methods of concentrating a cell population, as well as automated cell engineering systems that can utilize the cassettes and carry out the methods.

A polymer blend membrane includes a polyether-based copolymer and a polyether polymerized in situ and has high permeability and high selectivity for carbon dioxide. In the polymer blend membrane, the free volume of the polyether-based copolymer is greatly increased, and the adsorption capacity for carbon dioxide is enhanced. Thus, it can have excellent mechanical properties and excellent permeability and selectivity for carbon dioxide.

Disclosed is a 1D nanofibers quasi-aligned, grid structure cross-laminated, and pore distribution and size controlled 3D polymer nanofiber membrane, and manufacturing method thereof. A 3D polymer nanofiber membrane controlled in pore size and porosity is formed by employing an electrospinning pattern forming apparatus that includes double insulating blocks quasi-aligns nanofibers in a specific direction by transforming an electric field and includes a current collector rotatable in 90. Additionally, the 3D polymer nanofiber membrane may be used for air filters, separator, water filters, cell culture membranes, and so on by allowing various properties thereto through a functional surface coating.

The present invention relates to polymeric membranes. In particular, the present invention relates to the use of membranes comprising polyvinyl alcohol in electrophoresis.

The present invention relates to polymeric membranes. In particular, the present invention relates to the use of membranes comprising polyvinyl alcohol in electrophoresis.

A hollow fiber membrane contains a vinylidene fluoride-based resin and polyethylene glycol. In the hollow fiber membrane, the polyethylene glycol has a content of 1.0 part by weight or more and less than 5.0 parts by weight with respect to 100 parts by weight of the vinylidene fluoride-based resin. In a case where the hollow fiber membrane is divided in three equal parts by a line drawn from an inner surface side to an outer surface side of the hollow fiber membrane in a radial direction of a cross section perpendicular to a longitudinal direction of the hollow fiber membrane, and where polyethylene glycol normalized intensities at respective intermediate points are defined as inner surface part a, central part b, and outer surface part c, c is less than 0.3 and a is 0.5 or more.

A hollow fiber membrane contains a vinylidene fluoride-based resin and polyethylene glycol. In the hollow fiber membrane, the polyethylene glycol has a content of 1.0 part by weight or more and less than 5.0 parts by weight with respect to 100 parts by weight of the vinylidene fluoride-based resin. In a case where the hollow fiber membrane is divided in three equal parts by a line drawn from an inner surface side to an outer surface side of the hollow fiber membrane in a radial direction of a cross section perpendicular to a longitudinal direction of the hollow fiber membrane, and where polyethylene glycol normalized intensities at respective intermediate points are defined as inner surface part a, central part b, and outer surface part c, c is less than 0.3 and a is 0.5 or more.