Watersep Bioseparations LLC

Julie-Anne Burdick

Attila Herczeg

Bengt G Persson

Disclosed, herein is a single pass cross flow filtration system comprising: a filtration module, comprising two or more filtration segments fluidly connected in series, each having an upstream side and a downstream side; wherein each filtration segment comprises hollow fiber filter membranes, and wherein, when in use, the desired permeate flux is controlled by a configuration comprising: each filtration segment having a selected length; the hollow fiber filter membranes of each filtration segment, having a selected lumen diameter, wherein the selected inner diameter of each filtration segment may be the same or different, provided that at least one selected lumen diameter differs from another selected lumen diameter, and provided that the two or more filtration segments are arranged such that for a given filtration segment, having a selected lumen diameter, no filtration segment on the upstream side of the given filtration segment has a selected lumen diameter that is larger; and one or more pumps, mounted in the permeate channel.

Single pass cross flow filtration module and method

Disclosed herein is a perfusion filtration module or bioreactor for filtering a fluid, wherein the filtration module or bioreactor has a plurality of hollow fiber filter membranes that are splayed to reduce fouling of the filtration array.

Perfusion filtration system

Disclosed herein is a single pass cross flow diafiltration system comprising: a filtration module having; two or more filtration segments fluidly connected in series, each having an upstream side and a downstream side; wherein each filtration segment comprises hollow fiber filter membranes, and wherein each filtration segment has a selected length; wherein the hollow fiber filter membranes of each filtration segment have a selected inner diameter; wherein the selected inner diameter of each filtration segment may be the same or different, provided that at least one selected inner diameter differs from another selected inner diameter, and provided that the two or more filtration segments are arranged such that no selected inner diameter in a given filtration segment is larger on the upstream side; one or more pumps, mounted to urge fluid flow; and one or more points of introduction of a diadiluent, each of said points of introduction being fluidly connected to an upstream filtration segment.

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Hudson, MA, United States of America

Julie-Anne Burdick