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 high velocity cross flow dynamic membrane filtration system disc membrane assembly includes a frame having first and second end members and a plurality of rails extending between the first and second end members. At least two parallel support shafts are coupled to the frame, each support shaft defining a longitudinal axis about which is positioned a plurality of axially spaced membrane discs. The plurality of membrane discs associated with one of the at least two parallel support shafts is interspersed between the plurality of membrane discs associated with another of the at least two parallel support shafts. Each rail of the plurality of rails is configured to be received by a mounting rail within a vessel defining a treatment chamber. A permeate tube is coupled to each support shaft and in fluid communication with the membrane discs associated with that support shaft.

Methods for selecting a filter for a filtration process are described. Input data is received, and based on the input data, one or more filter characteristics for each of a plurality of filter candidates for a filtration process are identified. Process parameters of the filtration process are identified. A computer-implemented simulation process of the filtration process for each of the plurality of filter candidates is performed, based on the identified process parameters and identified filter characteristics. One or more output characteristics of the filtration process are determined based on the simulation. A filter candidate of the plurality of filter candidates is selected based on the one or more output characteristics.

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.

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

A device for filtering and separating pressurized liquid mixtures by means of a membrane includes a substantially pressure-tight container in which the membranes are accommodated in a pressure-tight manner. The container has at least one intake for the mixture, as well as at least one outlet for the permeate separated from the mixture by means of the membranes, and at least one outlet for the retentate, also referred to as a concentrate. The pressure-tight container is made of plastic.

The present invention relates to modification to permeate channels and permeate materials in a cross-flow filtration system to improve performance in counter current filtration having both retentate channels and permeate channels wherein a solution is pumped through one of the channels and drawn through a membrane to one of the other channels to assist in positive pressure driven filtration by using the osmotic pressure, concentration, or preferential solubility difference between the retentate and permeate flow streams thereby increasing or altering the flux through the membrane separating the flow streams.

The present invention relates to modification to permeate channels and permeate materials in a cross-flow filtration system to improve performance in counter current filtration having both retentate channels and permeate channels wherein a solution is pumped through one of the channels and drawn through a membrane to one of the other channels to assist in positive pressure driven filtration by using the osmotic pressure, concentration, or preferential solubility difference between the retentate and permeate flow streams thereby increasing or altering the flux through the membrane separating the flow streams.

A filter device (10), in particular for a tangential flow filtration device, has at least one fluid inlet (22), at least one retentate outlet (24) and at least one permeate outlet (26). The filter device (10) further has at least one membrane (16) which separates a retentate section (18) from a permeate section (20) in the filter device (10). Arranged in the retentate section (18) and/or in the permeate section (20) is at least one flow fitting (28) which is not formed from a woven or non-woven fabric, but from a structured plastic part, silicone part, metal part or ceramic part.

Provided is a filtration module for separating plasma from blood comprising a feeder channel lid, a feeder channel defined by a feeder channel laminating layer having a thickness of less than 5 mil, a filter element in fluid communication with the feeder channel and having a pore size of less than 2 microns and low surface area, and a filtrate take-off port having a dead volume of less than 10 L. Also provided are methods for filtering a blood sample comprising supplying the blood sample to a feeder channel of a filtration module and drawing the blood sample over a filter element of the filtration module in a single pass process configuration to provide a retentate and a plasma filtrate.