The invention relates to a membrane separation process for energy-efficient generation of oxygen from fresh air. In the process, mixed conducting membranes in vacuum operation are used, the fresh air is discharged as waste air after separation of the oxygen, at least 85% of the thermal energy required for heating the fresh air is acquired by utilizing the waste heat of the waste air and/or of the obtained oxygen, the rest of the heating of the fresh air being realized through external energy supply, and a ratio of fresh air to generated oxygen in normal operation is adjusted to a range of from 6:1 to 25:1.

A structure of assembly grasp for palladium-alloy tubes and the manufacturing method thereof are described. The structure of assembly grasp for palladium-alloy tubes includes a grasp with a plurality of holes, a plurality of palladium-alloy tubes inserted into the plurality of holes, and an intermetallic compound layer between the palladium-alloy tubes and the inner sidewalls of the plurality of holes.

A hydrogen separator having a first end plate, a second end plate, and a cylindrical support extending from the second end plate. A permeable tube support plate is suspended by the cylindrical support, wherein the second end plate, cylindrical support and permeable tube support plate define a collection chamber. A hydrogen permeable tube is coupled to the permeable tube support plate. A housing surrounds the cylindrical support. An exhaust tube support plate is within the housing and external of the collection chamber, wherein an exhaust chamber is defined between the exhaust tube support plate and the first end plate.

An oxygen gas supply device includes a tubular hydrated ion-exchange membrane defining an inner surface, an outer surface and an outlet. An outer catalytic membrane at the outer surface and an inner catalytic membrane at the inner surface are in electrical communication with a direct current power source. Application of electromotive force between the outer and inner catalytic membranes causes an oxygen gas component of the ambient air in contact with one or the other of the outer and inner catalytic membranes to be separated and collected at the other catalytic membrane and thereby be collected as an oxygen gas supply.

Systems and methods are provided that obtain the same or better level of performance by using lower operating flow rates, pressures and/or optimized flow distributions within the system. This extends the life of system components and lower energy consumption. In one embodiment, gas separation (or sieve) beds that are used to separate gaseous components are provided that have lower flow and pressure requirements compared to conventional beds. The sieve beds include, for example, a diffuser having low solid area in cross-section and maximum open area for flow while providing adequate mechanical properties to contain sieve material and support filter media. In another embodiment, systems and methods are provided having an indicator when a component has been serviced or repaired. This provides an indication whether the component has been tampered with in any manner. This allows the manufacturer to determine if the component was serviced, repaired, or tampered with outside the manufacturer's domain.

Provided are a gas separation membrane having a gas separation property and gas permeability and having heat resistance and pressure resistance even under an extremely high temperature and high pressure water vapor atmosphere, which is not a related-art product, a gas separation membrane module, and a gas permeable apparatus. A gas separation membrane according to the present embodiment includes a polyimide resin and a scaly filler. In a gas separation membrane module according to the present embodiment, the gas separation membrane is disposed in a closed container having a mixed gas inlet, a permeable gas outlet, and a non-permeable gas outlet. A gas permeable apparatus according to the present embodiment includes two or more gas separation membrane modules in which the above-described gas separation membrane is disposed in the closed container having the mixed gas inlet, the permeable gas outlet, and the non-permeable gas outlet.

A hydrogen-selective membrane including a metal leaf applied to a substrate. A system and method for fabricating a hydrogen-selective membrane, including applying a metal leaf to a substrate, annealing the metal leaf, applying a hydrogen-permeable metal to the annealed metal leaf on the substrate, and annealing the hydrogen-permeable metal and the annealed metal leaf to give an alloy of the hydrogen-permeable metal and the metal leaf. A system and method for repairing a hydrogen-selective membrane having defects including applying a metal leaf to an external surface of membrane material of the hydrogen-selective membrane, annealing the metal leaf and metal of the membrane material to form an alloy of the metal leaf and the metal to repair the defects.

A gas separation module and assembly for housing ceramic tubular membranes. The module includes a plurality of tubes containing the ceramic tubular membranes. The tubes are arranged parallel to one another and are supported by tube sheet plates at each end. Gas-tight seals surround each membrane, preventing a permeate gas within the inner lumen of the membrane from mixing with a feed or residue gas in the tube interior. The module also contains a gas distribution pipe for introducing feed gas into, and withdrawing residue out of, the module. This configuration allows for ceramic tubular membranes to be modularized for use in an assembly that carries out many types of gas separations.

A membrane capsule for biological and chemical separations comprising a cassette comprising an upper surface and a lower surface adjoined by a cassette sidewall, an inlet and an outlet located on the upper and lower surfaces of the cassette, tubes fluidly connected to the inlet and the outlet, holes or slots in the tubes to facilitate separation, and a membrane wrapped, pleated, and/or spiral wound around each of the tubes. Methods of separation comprising flowing fluid flow through the inlet of the membrane capsule, allowing the fluid to permeate through the holes or slots of the tubes, separating biological and/or non-biological substances, collecting the fluid within a reservoir, and draining fluid from the reservoir.

A separation membrane module includes a tubular housing, a columnar membrane structure housed in the housing and extending in a longitudinal direction, and an annular first flange surrounding a first end portion of the membrane structure. A first end surface of the membrane structure is located outward of an end surface of the first flange in the longitudinal direction.