B01D67/0055

COMPOSITE MOLECULAR SIEVE MEMBRANE, PREPARATION PROCESS AND USE THEREOF

A composite molecular sieve membrane, preparation method and use thereof are provided in the embodiments. The composite molecular sieve membrane includes a support layer and a molecular sieve membrane layer, wherein the support layer is a high-porosity and porous ceramic which is made of nano- or submicron ceramic powder materials or ceramic material precursors prepared through an electrospinning process. The high-porosity and porous ceramic, is adjustable from 40% to 83%. The composite molecular sieve membrane of the embodiments uses the porous ceramic prepared through an electrospinning process as the support layer, and the support layer has a flat and continuous surface, high porosity, uniform and adjustable pore sizes, low-tortuosity pore channels, and high mechanical strength; the flux of the composite molecular sieve membrane is increased, besides, the seed crystals can attach effectively due to the fibrous pore channels of the support layer, ensuring the adhesion amount of seed crystals.

Method to make carbon molecular sieve hollow fiber membranes

A method of making a hollow fiber carbon molecular sieve is comprised of heating a hollow polymer fiber to a carbonization temperature in an atmosphere that is non-oxidizing to form a hollow fiber carbon molecular sieve, wherein during at least a portion of the heating a tensile force is applied to the hollow polymer fiber. The method may improve the separation of gases similar in size such a propylene from propane.

METHOD FOR PRODUCING GAS SEPARATION MEMBRANE, AND GAS SEPARATION MEMBRANE

A method for producing a gas separation membrane includes a step of leaving a dispersion liquid to stand still, the dispersion liquid being obtained by mixing zeolite microcrystalline bodies formed from MFI zeolite and graphene oxide with pure water, and covering the periphery of the zeolite microcrystalline bodies with the graphene oxide; a step of drying the dispersion liquid after being left to stand to obtain a powder; a step of subjecting the powder to a reduction treatment of the graphene oxide by means of heating; and a step of pressure-forming the powder after the reduction treatment so as to be formed into a membrane form.

Perfluorocarbon-free membranes for membrane distillation

A perfluorocarbon-free membrane composed of a non-perfluorocarbon material having a first side and a second side opposite of the first side. The perfluorocarbon-free membrane also includes a plurality of pores, each having an inlet and outlet and each passing through the non-perfluorocarbon material so that each pore provides fluidic communication between the first and second sides of the non-perfluorocarbon material. A portion of the non-perfluorocarbon material extends over the inlet and outlet of each the plurality of pores so that a cross-sectional area of the inlets and outlets in a direction of the extension of the non-perfluorocarbon material is smaller than a cross-sectional area of the respective pore in the direction of the extension of the non-perfluorocarbon material. The perfluorocarbon-free membrane does not include a hydrophobic perfluorocarbon coating.

CARBON DIOXIDE MEMBRANE FILTER WITH GRAPHENE CROWN PORES
20230145516 · 2023-05-11 ·

A structure and method for carbon capture, e.g., in flue gas. An oxygen-terminated crown pore in graphene can be provided. Exposed carbon atoms on the pore edge can be bonded with oxygen to make a crown pore. When the CO.sub.2 is inside the pore, the electrostatic interaction becomes attractive because the positively charged carbon atom in CO.sub.2 is now exposed to negatively charged oxygen atoms on the crown pore edge. A favorable interaction between CO.sub.2 and the crown pore can be expected.

SELECTIVE INTERFACIAL MITIGATION OF GRAPHENE DEFECTS

A method for the repair of defects in a graphene or other two-dimensional material through interfacial polymerization.

CNT-based reverse osmosis desalination
11364472 · 2022-06-21 · ·

The present disclosure relates to nanochannel plates for use in reverse osmosis systems and methods of their manufacture. An example nanochannel plate includes a first surface and an opposing second surface. The first surface and the second surface are parallel to a major flat of the nanochannel plate. The nanochannel plate also includes a plurality of channels. At least one channel includes a carbon nanotube having a first end opening proximate to the first surface and a second end opening proximate to the second surface. Optionally, a core portion of the carbon nanotube could be configured to transport water from the first surface to the second surface or vice versa. Optionally, the core portion of the carbon nanotube has a core diameter of less than or equal to 0.7 nanometers.

METHODS OF PREPARING SOLID PARTICULATE MATERIALS

There is described a method of preparing solid particles of a compound, said method comprising controlling provision of a liquid phase, wherein said liquid phase comprises a solution of the compound, in a first flow direction to a membrane, said membrane defining a plurality of pores; and controlling the supersaturation of the liquid phase after it has passed through the membrane via the plurality of pores, to form solid particles of the compound. The method may comprise a continuous method.

Selective interfacial mitigation of graphene defects

A method for the repair of defects in a graphene or other two-dimensional material through interfacial polymerization.

PERFLUOROCARBON-FREE MEMBRANES FOR MEMBRANE DISTILLATION

A perfluorocarbon-free membrane composed of a non-perfluorocarbon material having a first side and a second side opposite of the first side. The perfluorocarbon-free membrane also includes a plurality of pores, each having an inlet and outlet and each passing through the non-perfluorocarbon material so that each pore provides fluidic communication between the first and second sides of the non-perfluorocarbon material. A portion of the non-perfluorocarbon material extends over the inlet and outlet of each the plurality of pores so that a cross-sectional area of the inlets and outlets in a direction of the extension of the non-perfluorocarbon material is smaller than a cross-sectional area of the respective pore in the direction of the extension of the non-perfluorocarbon material. The perfluorocarbon-free membrane does not include a hydrophobic perfluorocarbon coating.