B01D2053/223

Gas separation system and gas separation method
11779880 · 2023-10-10 · ·

A gas separation system for controlling a concentration of a first gas species and a second gas species in an outlet gas comprises a splitter unit. The splitter unit comprises a gas membrane system having a gas inlet port. The gas inlet port is in fluid connection with an air intake. A membrane is a selective barrier and allows some things to pass through but stops others.

ENERGY VAPOR EXCHANGER WITH AN INLET VORTEX GENERATOR
20230277981 · 2023-09-07 ·

A membrane assembly of an energy and vapor exchanger includes a gas-permeable membrane having a first major surface that faces a gas flow and a second major surface that faces a liquid desiccant flow. An inlet region is proximate an inlet edge of the gas-permeable membrane. The inlet region includes a vortex generator that creates a vortex in the gas flow as it moves from the inlet edge to an outlet edge of the gas-permeable membrane. The vortex enhances mixing of fluids along the gas-permeable membrane.

High temperature steam separation membrane

Ceramic proton-conducting oxide membranes are described herein, which are useful for separating steam from organic chemicals under process conditions. The membranes have a layered structure, with a dense film of the perovskite over a porous composite substrate comprising the perovskite material and a metallic material (e.g., Ni, Cu, or Pt). The perovskite comprises an ABO.sub.3-type structure, where “A” is Ba and “B” is a specified combination of Ce, Zr, and Y. The perovskite ceramic materials described herein have an empirical formula of Ba(Ce.sub.xZr.sub.1-x-nY.sub.n)O.sub.3-δ, wherein 0<x<0.8 (e.g., 0.1≤x≤0.7 or 0.2≤x≤0.5); and 0.05≤n≤0.2; and δ=n/2. In some embodiments n is about 0.2. In some other embodiments 0.6≤x≤0.8; and n is about 0.2, such as Ba(Ce.sub.0.7Zr.sub.0.1Y.sub.0.2)O.sub.3-δ, also referred to herein as BCZY712.

MOISTURE REMOVING DEVICE FOR A LAUNDRY APPLIANCE THAT INCORPORATES A NANOPORE MEMBRANE
20220395775 · 2022-12-15 · ·

A dehumidification mechanism for an appliance includes a blower that delivers humid process air along an airflow path. A drum is positioned along the airflow path. A condensing apparatus dehumidifies the humid air to define dehumidified air. A membrane has a plurality of nanopores that define a portion of the airflow path within the condensing apparatus. The humid air is delivered along the membrane having the plurality of nanopores and the nanopores operate through capillary condensation to dehumidify the humid air and separate condensate away from the humid air to define the dehumidified air. The condensate removed by the nanopore membrane is delivered away from the airflow path and to a condensate collection area within the appliance.

SINTERED POROUS BODY WITH MULTIPLE LAYERS
20230347300 · 2023-11-02 ·

Described are porous, sintered inorganic bodies that include multiple layers made from different types of metal particles, that may be useful as filter membranes, and also to methods of making and using the porous, sintered inorganic bodies.

Air separation modules, nitrogen generation systems, and methods of making air separation modules

An air separation module includes a canister, a separator, and a first end cap. The canister has an interior, a first open end in fluid communication with the interior of the canister, and a second end opposite the first open end of the canister. The separator is arranged within the interior of the canister, the separator fluidly coupling the second open end of the canister with the first open end of the canister. The first end cap has a one-piece first end cap body, is fixed to the first open end of the canister and has a first flange portion and a first aircraft-mounting portion. The canister supported by the first aircraft-mounting portion through the first flange portion of the one-piece first end cap body without an intermediate support structure. Nitrogen generation systems and methods of making nitrogen generation systems are also described.

ELECTROLYTIC SMELTING SYSTEM
20220243293 · 2022-08-04 ·

An electrolytic smelting system includes: an electrolytic smelting furnace including a furnace body to which a molten ore is introduced, a cathode substrate which is installed on a bottom portion in the furnace body, and an anode substrate which is positioned above the cathode substrate in the furnace body; an inert gas circulation unit including a circulation line to recover an inert gas supplied into the electrolytic smelting furnace together with oxygen and supply the inert gas to the molten ore; and an oxygen-removing unit which is installed in the circulation line and which removes oxygen from the circulation line.

Ultrathin Membrane Fabrication
20220219124 · 2022-07-14 ·

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.

HIGH TEMPERATURE STEAM SEPARATION MEMBRANE

Ceramic proton-conducting oxide membranes are described herein, which are useful for separating steam from organic chemicals under process conditions. The membranes have a layered structure, with a dense film of the perovskite over a porous composite substrate comprising the perovskite material and a metallic material (e.g., Ni, Cu, or Pt). The perovskite comprises an ABO.sub.3-type structure, where “A” is Ba and “B” is a specified combination of Ce, Zr, and Y. The perovskite ceramic materials described herein have an empirical formula of Ba(Ce.sub.xZr.sub.1-x-nY.sub.n)O.sub.3-δ, wherein 0<x<0.8 (e.g., 0.1≤x≤0.7 or 0.2≤x≤0.5); and 0.05≤n≤0.2; and δ=n/2. In some embodiments n is about 0.2. In some other embodiments 0.6≤x≤0.8; and n is about 0.2, such as Ba(Ce.sub.0.7Zr.sub.0.1Y.sub.0.2)O.sub.3-δ, also referred to herein as BCZY712.

GAS SEPARATION SYSTEM AND GAS SEPARATION METHOD
20220111330 · 2022-04-14 ·

A gas separation system for controlling a concentration of a first gas species and a second gas species in an outlet gas comprises a splitter unit. The splitter unit comprises a gas membrane system having a gas inlet port. The gas inlet port is in fluid connection with an air intake. A membrane is a selective barrier and allows some things to pass through but stops others.