A hybrid cooler/dryer that conditions a sample gas includes a heat exchanger, a condensate-removal device, and a membrane dryer. In some embodiments, the hybrid cooler/dryer also includes passive cooling, as embodied by an air amplifier and heat sink, or a length of tubing that exposes the sample gas to ambient temperature. The hybrid cooler/dryer requires no electrical power.

A fluid conduit includes a first portion having a first porosity, a second portion disposed immediately adjacent to the first portion, the second portion having a second porosity that is greater than the first porosity, and a third portion of the fluid conduit disposed immediately adjacent to the second portion, the third portion having a third porosity that is less than the second porosity. Each of the first portion, the second portion, and the third portion may be integrally formed as a single, continuous piece defining the fluid conduit.

Described are porous sintered metal bodies and methods of making porous sintered metal bodies by additive manufacturing methods.

A method is described for forming a body having at least one through-going passage, said method has the steps of: a) providing a mixture comprising particles and at least one liquid pocket inside a curable matrix, b) subjecting said mixture to a first alternating voltage having a first frequency to form a body in which said at least one liquid pocket extends from a first surface of said body to a second surface of said body thereby forming at least one through-going passage lacking curable matrix, and c) curing said curable matrix into a cured matrix, wherein at least some of said particles are located at an interface between said at least one through-going passage comprising liquid and said cured matrix.

A method for processing a fluid with forward osmosis process includes providing one or more tubular membranes each including a tubular nonwoven base layer on the outside of the tubular membrane forming an outer shell of the tubular membrane and providing a lumen for feed flow; a polymer substrate layer on the lumen-side of the tubular membrane comprising three regions, including a region where the polymer substrate layer is partially intruded into the tubular base layer, a region with an open macrovoid structure and a region with an asymmetrical foamy layer, where the partially intruded region forms an intermediate layer; and a functional top layer on the polymer substrate layer. The tubular base layer comprises a longitudinal weld. The method includes providing the feed flow through the lumen and providing a draw solution on the outer shell side of the tubular membrane; and processing the feed flow with the membrane.

A separation membrane module that is provided enables a bending load that is applied to a support member that supports ends of tubular separation membranes to be decreased and enables a seal member between the outer circumferential surface of the support member and the inner circumferential surface of a housing to be omitted. The separation membrane module includes a tubular housing 2, tubular separation membranes 3 that are arranged in a longitudinal direction of the housing 2, end tubes 4 that are connected to the lower ends of the tubular separation membranes 3, a support box 5 that supports the end tubes 4, and a backpressure chamber 16 below the support box 5. The tubular separation membranes 3 are in communication with a collection chamber 5v of the support box 5. A permeated fluid is extracted via a nozzle 5n that is disposed on the support box 5. A chamber 11 and the backpressure chamber 16 are in communication with each other via a gap between the outer circumferential surface of the support box 5 and the inner circumferential surface of the housing 2. Pressure in the chamber 11 and pressure in the chamber 16 are substantially the same.

A separation membrane module that is provided enables a bending load that is applied to a support member that supports ends of tubular separation membranes to be decreased and enables a seal member between the outer circumferential surface of the support member and the inner circumferential surface of a housing to be omitted. The separation membrane module includes a tubular housing 2, tubular separation membranes 3 that are arranged in a longitudinal direction of the housing 2, end tubes 4 that are connected to the lower ends of the tubular separation membranes 3, a support box 5 that supports the end tubes 4, and a backpressure chamber 16 below the support box 5. The tubular separation membranes 3 are in communication with a collection chamber 5v of the support box 5. A permeated fluid is extracted via a nozzle 5n that is disposed on the support box 5. A chamber 11 and the backpressure chamber 16 are in communication with each other via a gap between the outer circumferential surface of the support box 5 and the inner circumferential surface of the housing 2. Pressure in the chamber 11 and pressure in the chamber 16 are substantially the same.

A porous cylindrical support for use in supporting a zeolite membrane has a generally cylindrical inside surface having a central axis extending in the longitudinal direction and a generally cylindrical outside surface that surrounds the inside surface. A zeolite membrane is formed on the outside surface. A maximum value A and a minimum value B of a support thickness in a circumferential direction satisfy (A−B)/(A+B)≤0.3 in at least part of the support in the longitudinal direction, the support thickness being a radial distance between the inside surface and the outside surface. By reducing a variation in support thickness, it is possible to improve uniformity in the thickness of the zeolite membrane formed on the support.

A porous cylindrical support for use in supporting a zeolite membrane has a generally cylindrical inside surface having a central axis extending in the longitudinal direction and a generally cylindrical outside surface that surrounds the inside surface. A zeolite membrane is formed on the outside surface. A maximum value A and a minimum value B of a support thickness in a circumferential direction satisfy (A−B)/(A+B)≤0.3 in at least part of the support in the longitudinal direction, the support thickness being a radial distance between the inside surface and the outside surface. By reducing a variation in support thickness, it is possible to improve uniformity in the thickness of the zeolite membrane formed on the support.

A method of joining and sealing a vanadium based membrane to a metallic connection section comprising: mounting a section of a vanadium based membrane on a connector formation of a connection section, the connection section being formed of a different metal to the vanadium based membrane, the connector formation providing a recess into which a section of the vanadium based membrane is seated and a connection interface in which the end face of the vanadium based membrane is proximate to or substantially abuts an adjoining face of the connector formation; mounting and operating a chiller arrangement in thermal contact with vanadium based membrane proximate the connection interface; heating a filler metal on the connection section to at least the liquidus temperature of the filler metal using a laser beam directed onto the filler metal located on the connection section and having a beam edge positioned at an offset location spaced apart from the connection interface a distance that attenuates direct heating of the vanadium based membrane by the laser beam, and on the connection section, such that the filler metal can flow over the connection interface from the offset location onto the vanadium based membrane; and cooling the filler metal to form a bridging section of filler metal between the vanadium based membrane and connection section over the connection interface.