A crystalline material contains oxygen, aluminum and phosphorus, and has powder X-ray diffraction peaks shown below. When the peak at 2θ=14.17±0.2° is used as the reference peak and the intensity of the reference peak is set to 100, for example, the relative intensity of the peak at 2θ=8.65±0.2° is 1 to 15. The relative intensity of the peak at 2θ=9.99±0.2° is 1 to 15. The relative intensity of the peak at 2θ=16.52±0.2° is 5 to 80. The relative intensity of the peak at 2θ=17.37±0.2° is 1 to 15. The relative intensity of the peak at 2θ=21.81±0.2° is 10 to 80.

A mixed gas separation method includes supplying a mixed gas containing at least N.sub.2, H.sub.2, and CO.sub.2 and having a CO.sub.2 concentration of 30% or less by volume to a first separation membrane that selectively allows passage of H.sub.2, supplying the first non-permeated gas to a second separation membrane that selectively allows passage of CO.sub.2, and supplying the second non-permeated gas to a CO.sub.2 collector that separates and collects CO.sub.2 by a separation method other than membrane separation to collect CO.sub.2 contained in the second non-permeated gas. The first non-permeated gas has a CO.sub.2 concentration that is 5% or more by volume higher than or equal to the CO.sub.2 concentration in the mixed gas. The second non-permeated gas has an N.sub.2 concentration of 50% or more by volume and an H.sub.2 concentration of 30% or less by volume.

A hydrogen bonded organic framework (HOF) includes at least one kind of organic linker with at least one functional group forming a hydrogen-bonded network, the functional group includes a hydroxyl group and a central atom of tetrahedral geometry, the HOF is semi-conductive, proton-conductive and porous, and can even be microporous. In some embodiments, the at least one functional group is phosphonic acid, phosphinic acid, arsonic acids, arsinic acids, phosphonate, arsonate and/or esters thereof including at least one hydroxylgroup. A covalent organic framework (COF), is also provided based on an HOF for transforming the hydrogen bonds between the functional groups into covalent anhydride bonds via a condensation reaction or reactions known to form anhydrides.

Disclosed herein are vapour-phase crosslin ked composite membranes in the form of crosslinked polymers and defined inorganic materials. The membranes disclosed herein may have a narrow pore size distribution and precise molecule separation ability and may be used for organic solvent nanofiltration and organic solvent reverse osmosis. Also disclosed herein are methods of forming the membranes, and filtration. In a preferred embodiment, the vapour-phase crosslinked composite membrane is obtained by exposing a composite membrane comprising polyimide and UiO-66-NH.sub.2 particles to an amine vapour.

A carbon molecular sieve (CMS) membrane having improved separation characteristics for separating olefins from their corresponding paraffins is comprised of carbon with at most trace amounts of sulfur and a group 13 metal. The CMS membrane may be made by pyrolyzing a precursor polymer devoid of sulfur in which the precursor polymer has had a group 13 metal incorporated into it, wherein the metal is in a reduced state. The pyrolyzing for the precursor having the group 13 metal incorporated into it is performed in a nonoxidizing atmosphere and at a heating rate and temperature such that the metal in a reduced state (e.g., covalently bonded to carbon or nitrogen or in the metal state).

Membranes, methods of making the membranes, and methods of using the membranes are described herein. The membranes can comprise a support layer, and a selective polymer layer disposed on the support layer. The selective polymer layer can comprise a selective polymer matrix and carbon nanotubes dispersed within the selective polymer matrix. The carbon nanotubes can comprise multi-walled carbon nanotubes wrapped in a hydrophilic polymer, such as polyvinylpyrrolidone or a copolymer thereof, such as poly(1-vinylpyrrolidone-co-vinyl acetate). The membranes can exhibit selective permeability to gases. As such, the membranes can be for the selective removal of carbon dioxide and/or hydrogen sulfide from hydrogen and/or nitrogen.

Embodiments include a filter material including an electrospun nanofiber membrane and an active nanomaterial agent incorporated into the electrospun nanofiber membrane, wherein the electrospun nanofiber membrane filters disease-causing agents and the wherein the active nanomaterial agent degrades disease-causing agents. Embodiments further include a face mask and/or respirator including a filter material, wherein the filter material includes an electrospun nanofiber membrane and an active nanomaterial agent incorporated into the electrospun nanofiber membrane, wherein the electrospun nanofiber membrane filters disease-causing agents and the wherein the active nanomaterial agent degrades disease-causing agents.

A gas separation membrane selectively permeable to a specific gas component includes a first porous layer, and a separation function layer provided on a first surface of the first porous layer. The separation function layer contains a hydrophilic resin. The first surface has a wetting tension of greater than or equal to 38 mN/m and less than or equal to 52 mN/m.

The present disclosure describes membrane compositions and methods for preparing membrane compositions. In particular, the methods employ a layer-by-layer approach to membrane preparation. The membrane compositions provide significantly enhanced membrane performance over existing commercial membranes, particularly in terms of permeability and selectivity.

The invention includes compositions and methods for promoting gas mixtures separations, such as a carbon dioxide and methane mixture. The composition of the invention is based on a curable polymerized room-temperature ionic liquid [poly(RTIL)].