A fluid filtration assembly includes a filter housing having a first end for fluid connection with a fluid storage vessel. A filter cartridge is disposable within the filter housing, and a plunger pump is coupled at a second end of the filter housing. The plunger pump includes a housing having a rigid portion and a flexible portion. The flexible portion has a plunger-engaging portion for coupling to the plunger of an actuator. The flexible portion selectively movable with respect to the rigid portion via the actuator. The filter cartridge can be a hollow fiber filter. The plunger pump can be configured to induce alternating tangential flow in at least a portion of the assembly. The fluid filtration assembly can be provided as a disposable single-use arrangement.

The present disclosure provides systems and methods for bioprocessing. The systems and methods can be implemented using a chip (solid support comprising a bioprocessing chamber). The bioprocessing chamber can be fluidically connected to a feeding input channel. The chip can permit a fluid to flow from the feeding input channel through the bioprocessing chamber for cell seeding, perfusion, and/or expansion. The bioprocessing chamber can be in fluidic communication with a collection output. The cells can be harvested from the bioprocessing chamber through the collection output.

A method of controlling a bioreactor system includes providing a cell culture in a bioreactor, wherein conditions in the bioreactor enable the cell culture to produce a protein of interest (POI), measuring process parameters (PPs) of the culture within the bioreactor by RAMAN, wherein the process parameters are selected from the group consisting of nutrient concentration, viable cell concentration, and protein attributes, measuring a predetermined weight of the bioreactor with the cell culture, removing cell-free spent media from the cell culture using a first output conduit at a first specified rate, removing cells from the cell culture using a second output conduit at a second specified rate, and introducing one or both of fresh media or nutrients into the cell culture using an input conduit at a third specified rate.

A cell culture apparatus includes one or more plates having a first major surface and an opposing second major surface. The first major surface comprises a structured surface defining a plurality of wells. Each well has an interior surface defining an upper aperture and a nadir, wherein the upper aperture of each well has a diametric dimension in a range from 100 micrometers to 2000 micrometers. The apparatus also includes a plurality of spacers extending from the first major surface along a length of the bottom surface. A plurality of flow channels are defined between adjacent rails.

A continuous flow system for passing fluid over a biofilm to simulate an oral environment is described. In one embodiment, the continuous flow system includes a plurality of channels fluidly connected by one or more channel connectors, an inflow conduit defining an inflow channel and an outflow conduit defining an outflow channel. The plurality of channels can receive the fluid via the inflow conduit from a reservoir positioned upstream of the flow cell housing and the outflow channel can receive the fluid from the plurality of channels.

A system and method are provided for harvesting target biological substances. The system includes a substrate and a first and second channel formed in the substrate. The channels longitudinally extending substantially parallel to each other. A series of gaps extend from the first channel to the second channel to create a fluid communication path passing between a series of columns with the columns being longitudinally separated by a predetermined separation distance. The system also includes a first source configured to selectively introduce into the first channel a first biological composition at a first channel flow rate and a second source configured to selectively introduce into the second channel a second biological composition at a second channel flow rate. The sources are configured to create a differential between the first and second channel flow rates to generate physiological shear rates along the second channel that are bounded within a predetermined range.

The present disclosure relates to settling devices for separating particles from a bulk fluid with applications in numerous fields. The particle settling devices of the present disclosure may include a stack of truncoconical cones that may be arranged in opposite orientation, apex to base. Other embodiments include several concentric vertical tubes attached to conical surfaces at the bottom, with inclined settling strips attached to the vertical tubes in annular regions between the tubes. These devices are useful for separating small (millimeter or micron sized) particles from a bulk fluid with applications in numerous fields, such as biological (microbial, mammalian, plant, insect or algal) cell cultures, solid catalyst particle separation from a liquid or gas and waste water treatment.

The present invention relates to cell culture in bioreactors, such as flexible cellbag bioreactors. More closely the invention relates to a method and system for determining the cell density in a bioreactor culture and for controlling the perfusion rate of a suspension culture of cells in a bioreactor, comprising measuring the oxygen uptake of primary mononuclear cells in a non-static bioreactor.

A cell culture apparatus includes one or more plates having a first major surface and an opposing second major surface. The first major surface comprises a structured surface defining a plurality of wells. Each well has an interior surface defining an upper aperture and a nadir, wherein the upper aperture of each well has a diametric dimension in a range from 100 micrometers to 2000 micrometers. The apparatus also includes a plurality of spacers extending from the first major surface along a length of the bottom surface. A plurality of flow channels are defined between adjacent rails.

A microfluidic system for cell retention for a perfusion bioreactor is provided. The system comprises at least one inlet configured to receive a bioreaction mixture to be processed. At least one curvilinear microchannel is in fluid flow connection with the at least one inlet, the at least one curvilinear microchannel being adapted to isolate cells in the bioreaction mixture, based on cell size, along at least one portion of a cross-section of the at least one curvilinear microchannel. At least two outlets are in fluid flow connection with the at least one curvilinear microchannel. At least one outlet of the at least two outlets is configured to flow the isolated cells to be recycled to the perfusion bioreactor.