Disclosed herein is a gas separation section for separating a first gas from one or more other gasses in a separation device, the gas separation section comprising: a first membrane that is substantially planar; a second membrane that is substantially planar; a first substrate that has a first surface and a second surface, wherein the second surface of the first substrate is on an opposite side of the first substrate than the first surface of the first substrate; a second substrate that has a first surface and a second surface, wherein the second surface of the second substrate is on an opposite side of the second substrate than the first surface of the second substrate; and a mesh that is arranged between the second surface of the first substrate and the second surface of the second substrate; wherein: the first substrate and the second substrate are sintered plates; the first membrane is on the first surface of the first substrate; the second membrane is on the first surface of the second substrate; the first and second membranes are both permeable by at least a first gas and not permeable by one or more other gasses; the thickness of the first membrane in a direction orthogonal to the plane of the first membrane is less than 10 micrometres; and the thickness of the second membrane in a direction orthogonal to the plane of the second membrane is less than 10 micrometres. Embodiments provide an improved gas separation device over known techniques. Advantages of the separation device according to embodiment include improved performance, easy implementation, a modular design and a scalable design.

The present disclosure is directed to ion-exchange systems and devices that can monitor key parameters related to the performance of the ion-exchange device. Specifically, the ion-exchange systems and devices disclosed herein can provide real time voltage drop across groups of membrane pairs using diagnostic spacer borders between the pairs. In addition, the ion-exchange systems and devices disclosed herein can monitor the compression force applied by the compression plates holding the ion-exchange systems and devices together.

An automated continuous purification system includes a base and a plurality of purifying elements. The base includes a first flowing channel layer, a steering valve, a plurality of second flowing channel layers, a plurality of third flowing channel layers and a top layer. The first flowing channel layer includes a plurality of first flowing channels. The steering valve is disposed on a side of the first flowing channel layer and includes a plurality of through-holes. The second flowing channel layers are disposed on a side of the steering valve away from the first flowing channel layer. The third flowing channel layers are alternately stacked with the second flowing channel layers, and each of the third flowing channel layers is disposed on a side of each of the second flowing channel layers away from the steering valve. The top layer includes a plurality of inlets and a plurality of outlets.

An automated continuous purification system includes a base and a plurality of purifying elements. The base includes a first flowing channel layer, a steering valve, a plurality of second flowing channel layers, a plurality of third flowing channel layers and a top layer. The first flowing channel layer includes a plurality of first flowing channels. The steering valve is disposed on a side of the first flowing channel layer and includes a plurality of through-holes. The second flowing channel layers are disposed on a side of the steering valve away from the first flowing channel layer. The third flowing channel layers are alternately stacked with the second flowing channel layers, and each of the third flowing channel layers is disposed on a side of each of the second flowing channel layers away from the steering valve. The top layer includes a plurality of inlets and a plurality of outlets.

A humidifier has a plurality of humidifier modules that are clamped between end plates by tie rods and have a membrane that is permeable to water vapor, in which on both sides of the membrane there is respectively arranged a flow field frame having a multiplicity of webs defining a flow field. The tie rods are configured as hollow rods forming coolant tubes for a coolant to be led through. A fuel cell device and a motor vehicle having such a humidifier are also provided.

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.

A filtration cassette including a multilaminate array of sheets including filter sheets alternating with permeate sheet members and retentate sheet members, and a cross-flow filter device comprising a multiplicity of stacked filtration cassettes of such type. The improvements associated with the filtration cassettes described herein include, but are not limited to, at least one of: reinforced inlet(s) providing for longevity and improved cleanability of the cassettes; spacer permeate screens to limit throughput restriction; stainless steel or otherwise stiffened permeate sheets to prevent movement and increase flux; and stainless steel permeate sheets that can be used with ultrasonic transmission to minimize fouling of the filter sheets and extend cleaning cycles. Advantageously, the filtration cassettes are more resistant to higher temperatures than the filtration cassettes of the prior art.

A cross flow filtration unit, which provides a planar, rigid filter plate for filtration of liquid media. The plate has a planar membrane, which is fluid tight bonded at its edges to the surface of a partly hollow supporting plate having exit openings, internal flow channels, and flow areas for a first liquid medium. The membrane is in fluid contact with said the liquid medium at its internal surface and being in fluid contact with a second liquid medium at its external surface.

The present disclosure is directed to affinity chromatography devices including a fibrillated polymer membrane that contains inorganic particles having a spherical shape and a particle size distribution that has a D90/D10 less than or equal to 3. A blend or a combination of spherical inorganic particles may be utilized. A nominal particle size of the spherical inorganic particles is from about 5 microns to about 20 microns. An affinity ligand may be bonded to the spherical inorganic particles and/or to the fibrillated polymer membrane. Also, the affinity chromatography devices have a hydraulic permeability from about 100 (×10.sup.−12 cm.sup.2) to about 500 (×10.sup.−12 cm.sup.2). Additionally, the affinity chromatography devices have a cycling durability of at least 100 cycles without exceeding an pressure of 0.3 MPa. Manifolds containing multiple affinity chromatography devices in a parallel configuration and multiple manifolds in a parallel configuration are also disclosed.

A contactor system includes a plurality of contactor panels. Each contactor panel includes a frame member and a membrane array adapted to be received within the frame member. The membrane array defines a first end portion, a second end portion, and a plurality of hollow fibers. The contactor system also includes a first manifold in selective fluid communication with the first end portion of the membrane array of each contactor panel. The contactor system further includes a second manifold in direct fluid communication with the second end portion of the membrane array of each contactor panel. The contactor system includes a controller configured to provide selective fluid communication between the first manifold and the first end portion of the membrane array of each contactor panel.