Material transfer devices and related systems and methods are disclosed. In accordance with an example, a material transfer device includes a housing including a first housing portion and a second housing portion and a screen. The first housing portion includes a first inlet port, a first outlet port, and a first transfer opening. The second housing portion has a second inlet port, a second outlet port, and a second transfer opening. The first transfer opening is disposed adjacent to and in communication with the second transfer opening. The screen is disposed between the housing portions adjacent to the first and second transfer openings.

The present invention relates to a process for preparing ammonium (meth-) acrylate, aqueous ammonium (meth-) acrylate solutions obtainable by such process, and (meth-) acrylic acid homopolymers or copolymers obtainable by polymerizing such ammonium (meth-) acrylate. The invention furthermore relates to a modular, relocatable bioconversion unit for manufacturing aqueous ammonium (meth-) acrylate solutions.

The invention relates to a bioprocessing system having a main line (2) for conduction of a main flow (3) of a liquid, in particular biological, medium (45), having a main flow pump (5) for generation of the main flow (3) and having a system part (46) connected to the main line (2). What is proposed is that the bioprocessing system (1) comprises a powder transfer system (8) for metered delivery, in particular dust-free metered delivery, of an additive (47) and a feed line (9) which is connected to the powder transfer system (8) and which opens into the main line (2) at a feed point (10) and which comprises a return flow preventer (11) for prevention of a return flow of liquid medium (45), that the powder transfer system (8) feeds the additive (47) into the feed line (9) in powder form and drives it toward the feed point (10) by means of a pressurized transport gas (12) and that at least some of the fed additive (47) is input into the liquid medium (45) within the main line (2) downstream of the feed point (10) before the liquid medium (45) enriched with the additive (47) passes through or reaches the system part (46) connected to the main line (2).

A process for fermenting syngas is provided which is effective for decreasing an amount of time needed to inoculate a main reactor. The process includes propagating a culture of acetogenic bacteria to provide an inoculum for a main reactor and fermenting syngas in the main reactor.

We have found a way to make possible large-scale plasmid transfection using PEI to produce high titer viral vectors in fixed bed or adherent cell culture bioreactors by using PEI as a transfection agent, while avoiding formation of the PEI-plasmid precipitate which in prior art approaches clogged adherent bioreactor substrates. We have also found a way to improve PEI-based transfection by modifying how pH and CO.sub.2 are managed during transfection.

The present disclosure provides a special culture apparatus for a 3D biological tissue, and a method for preparing block-shaped cultured meat. The special culture apparatus for a 3D biological tissue includes: a 3D biological tissue culture tank for accommodating a 3D biological tissue, and a liquid storage tank for containing a culture medium; the 3D biological tissue culture tank is connected to the liquid storage tank by means of a pipeline to form a circuit for the culture medium to circularly flow; and an opening of the 3D biological tissue culture tank is provided with a sealing plug, an inner side of the sealing plug is provided with a plurality of culture medium infusion needles that penetrate the 3D biological tissue when in use.

Methods and apparatus of bioreactors for therapeutic cells manufacturing are provided herein. In some embodiments, a bioreactor includes: an upper bioreactor reservoir configured to perform multiple cell therapy manufacturing process steps including genetic modification and expansion to a plurality of cells disposed therein, wherein the upper bioreactor reservoir includes a plurality of ports for delivering fluids into and out of the upper bioreactor reservoir; a lower bioreactor compartment configured to hold a suspension comprising a molecular species; and a membrane disposed between the lower bioreactor compartment and the upper bioreactor reservoir, wherein the membrane includes a plurality of micro-straws extending through the membrane and into the upper bioreactor reservoir to transfect the plurality of cells with the molecular species.

A multiport device for connecting a loop, preferably a tangential flow filtration loop or a sensor loop, to one port of a bioreactor, preferably a single-use bioreactor, is configured to be fixed to the port of the bioreactor. The multiport device includes a first flow path configured for withdrawing fluid from the bioreactor, and a second flow path configured for supplying fluid to the bioreactor. The first flow path has a first end adapted to be in fluid connection with the bioreactor, and a second end adapted to be connected to an inlet of the loop. The second flow path has an outer end adapted to be connected to an outlet of the loop, and a mouth adapted to be in fluid connection with the bioreactor. The mouth of the second flow path is distanced from the first end of the first flow path by at least 5 mm, preferably 10 mm.

In one embodiment, a concentrically baffled reactor includes an outer housing that defines an interior space, an inlet through which material can be delivered into the interior space, an outlet through which material can be removed from the interior space, and multiple concentric baffles within the interior space that define multiple concentric reactor zones through which the material can sequentially flow to the outlet.

The present invention relates to a process for providing a first reaction product by a first fermentation process conducted in a first Loop reactor, the method comprising the steps of: (i) adding an inoculum comprising one or more methanogenic microorganism to the first Loop reactor providing a first inoculated fermentation medium; (ii) adding a gaseous hydrogen (H.sub.2) to the first inoculated fermentation medium; (iii) adding a first carbon source to the first inoculated fermentation medium; (iv) allowing the first fermentation medium to ferment, providing the first reaction product; and (v) isolating the first reaction product provided in step (iv).