The present invention relates to a method for dynamic filtration of a cross-linked biopolymer-based hydrogel to remove unwanted molecules from the gel. In particular, the invention relates to dynamic filtration of a hyaluronic acid hydrogel using a dynamic filtration construction with rotating and semipermeable filter discs.

A substrate for a composite membrane includes a microporous polyolefin membrane for carrying a hydrophilic resin compound within the pores of the microporous membrane wherein: the average pore diameter is 1 nm to 50 nm; the porosity is 50% to 78%; the membrane thickness is 1 μm to 12 μm; and, when a mixed solution of ethanol and water (volume ratio ½) is dripped onto a surface of the microporous polyolefin membrane which has not undergone hydrophilization treatment, the contact angle θ1 between the droplet and the surface is 0 to 90 degrees 1 second after the dripping, and the contact angle θ2 between the droplet and the surface is 0 to 70 degrees 10 minutes after the dripping, and the rate of change of the contact angle ((θ1−θ2)/θ1×100) is 10 to 50%.

This disclosure provides a method for concentrating a solution of a macromolecule that is retained on at least two semi-permeable membranes that have different molecular weight cutoffs (MWCOs), the method comprising passing the solution through a hybrid configuration of said semi-permeable membranes staged in series in a single pass tangential flow filtration (SPTFF) apparatus. The method is applicable to the efficient concentration of biological macromolecules such as proteins, antibodies and nucleic acids.

A water-permeable device. The device has a supporting layer and a water-permeable membrane. The water-permeable membrane includes graphene layers that are aligned to form interlayer hydrophobic channels between the graphene layers. The interlayer hydrophobic channels are positioned to be aligned with the direction of water permeation. Also disclosed are systems and methods for water treatment.

The present disclosure relates to a method for separating an organic zinc catalyst dispersed in a polyalkylene carbonate resin solution by filtering the polyalkylene carbonate resin solution using a composite filtering membrane, which is a composite material comprising a hydroxyl group-containing material and polyolefin material and has a form in which one or both surfaces of the polyolefin material is coated with the hydroxyl group-containing material.

A device for exchange of water molecule and temperature between two fluids. The device comprises thin molecular sieve membrane sheets that allow water molecules to permeate through while blocking cross-over of the exchanging fluids. The device provides two sets of flow channels having a hydraulic diameter ranged from 0.5 to 2.0 mm for respective process and sweep fluid flows. The two sets of the channels are separated by a membrane sheet having a thickness less than 200 μm. The thin molecule sieve membrane may be prepared by forming an ultra-thin zeolite membrane layer on a porous metal-based support sheet which provides very high water permeance so that the exchange can be conducted in a compact membrane module at high throughput. The device can be used to remove water from a process stream of higher water content by use of a sweep fluid of lower water content or higher water affinity. For example, the device can be used to condition outdoor fresh air close to the temperature and humidity of indoor air by conducting humidity and heat exchange between the fresh air flow drawn from outdoors and waste air discharged indoors.

A system for treatment of a polluted effluent includes an outer chamber and a computerized control system. The system is configured to treat an effluent/catalyst mixture that includes the polluted effluent in admixture with a purification slurry. The slurry includes particles of one or more catalysts and/or organoclays. The treatment of the effluent/catalyst mixture is carried out by contact between the particles of the catalysts and/or organoclays and the polluted effluent to mineralize or degrade pollutants in the polluted effluent.

In one or more embodiments, a battery may include one or more cells and one or more enclosures that respectively enclose the one or more cells. For example, at least a portion of each enclosure of the one or more enclosures may include a zeolite material that is configured to permit first molecules associated with a first diameter to exit the enclosure and configured to inhibit second molecules associated with a second diameter, greater than the first diameter, from entering the enclosure. In one instance, the first molecules may include CO.sub.2 molecules. In another instance, the second molecules may include H.sub.2O molecules. In one or more embodiments, the zeolite material may be a DDR-type zeolite material. For example, the DDR-type zeolite material may be applied on a porous α-alumina substrate. In one or more embodiments, the battery may provide power to one or more components of an information handling system.

A nanopore sensing system includes a cis well, a trans well, and a metal based membrane positioned between the cis and trans wells so that a channel defined in the metal based membrane fluidically connects the cis and trans wells. The metal based membrane has a thickness ranging from about 1 nm to about 3 nm and is selected from the group consisting of a metal oxide, a metal sulfide, a metal nitride, a metal phosphide, a metal arsenide, a metal antimonide, a metal selenide, and a metal telluride.

The inventions discloses a method for reducing fouling on the surface of a ceramic membrane or filter with a recalcitrant filtration cake thereon that is non-responsive to regular back-flushing or other physical means of removal, where the ceramic membrane or filter is subjected to steam fast-flushing by injecting steam directly in feed channel of the ceramic membrane or filter while back-flushing the ceramic membrane or filter at the same time to heat and remove fouled layer on the ceramic membrane or filter while cooling a selective layer of the ceramic membrane or filter to avoid thermal shocking of the ceramic membrane or filter, the surface is cleaned with the ceramic membrane or filter being stationary.