Embodiments described herein generally provide for the scheduled feeding of cells in a cell expansion system. A schedule to proactively and automatically increase and/or maintain inlet rates of media to feed cells may be created, in which inlet rates to the intracapillary portion (or extracapillary portion) of a bioreactor may be increased or maintained according to the schedule. Such schedule may be conservative or aggressive or a combination thereof, for example. Multiple schedules may be used. Scheduled media exchanges may also be included. By following a feed schedule, the monitoring of metabolite levels may be optional. Inlet rates may be increased or maintained without manual manipulation. Media usage may also be more predictable. In an embodiment, a custom task(s) may be created to follow a desired feed schedule. In another embodiment, a pre-programmed task(s) may be used for the scheduled feeding of cells.

Provided herein are tubular membrane filter elements, tangential flow filtration systems comprising such filter elements and methods of using such filter elements and filtration systems.

The invention provides methods and materials for culturing mammalian cells and harvesting recombinant protein.

Algae harvesting and cultivating systems and methods for producing high concentrations of algae product with minimal energy. In an embodiment, a dead-end filtration system and method includes at least one tank and a plurality hollow fiber membranes positioned in the at least one tank. An algae medium is pulled through the hollow fiber membranes such that a retentate and a permeate are produced.

The present disclosure relates to hollow fiber tangential flow filters, including hollow fiber tangential flow depth filters, for various applications, including bioprocessing and pharmaceutical applications, systems employing such filters, and methods of filtration using the same.

The present invention provides improved bioprocessing systems and methods for cell culture using the improved bioreactors, e.g., batch-fed or perfusion bioreactor cell culture systems for production of monoclonal or bi-specific antibodies, which are modified to include one or more membrane gas transfer modules in place of a sparger- or microsparger-based aeration systems to better regulate the levels of critical gases in a bioreactor cell culture, e.g., the dissolved levels of O2 and CO2, even at high cell densities, without subjecting the cells to bubble-burst associated cell death.

A cell culture bioreactor has perfusion membranes and gas transfer membranes or a gas phase in an extra-membrane space in contact with a film on the perfusion membranes. Gas transfer membranes may travel through the perfusion membranes or through the extra-membrane space. Examples with hollow fiber and flat sheet membranes are shown. One or more of the membranes optionally has a responsive surface, for example a thermo-responsive surface. In some examples, membranes are located in X-Y planes while the length of the reactor extends in a Z-direction.

The present invention relates to an anaerobic process for biogas upgrading and hydrogen utilization comprising the use of acidic waste as co-substrate. In this process, H.sub.2 and CO.sub.2 will be converted to CH.sub.4, which will result in lower CO.sub.2 content in the biogas. The invention relates to both in situ and ex situ methods of biogas upgrading. The invention further relates to a bioreactor comprising hollow fibre membranes.

The present disclosure relates, at least in part, to a closed and semi-automated system for the isolation of naive T cells, their expansion, and/or final harvest. The disclosure also relates to using those isolated cells in a large batch format for compiling stocks of stimulated CD45A+ T cells and/or using the stimulated CD45A+ T cells for therapeutic purposes.

A biological component treatment system according to embodiments of the present disclosure includes an IC route through which the liquid is capable of flowing in inner cavities of hollow fibers, and an EC route through which the liquid is capable of flowing in a main space on an outer side of the hollow fibers. The biological component processing system is further equipped with a control unit that controls a flowing state of the liquid through the IC route and the EC route. The control unit, at a time of priming, while the liquid flows through both the IC route and the EC route, causes a differential pressure to be generated between the liquid flowing through the inner cavities and the liquid flowing through the main space, and causes the gas to flow out from the hollow fibers.