A conjugation device includes at least one flow reactor having an inlet and an outlet, the flow reactor(s) being completely filled with a support such as a matrix including 1) chromatography beads, fibers or membranes, and 2) a biologic catalyzer, namely the enzyme ligase, which is immobilized onto this support; a fluid delivery unit in fluid communication with the inlet of the flow reactor(s) and configured to continuously provide the flow reactor(s) with at least one kind of reaction fluid such as antibody and linker-payload according to stages of the conjugation process, the at least one kind of process fluid including a first moiety and a second moiety of a conjugate to be produced; and a fluid collection unit in fluid communication with the outlet of the flow reactor(s) and configured to control collection of fluid flowing out of the outlet of the flow reactor(s) according to the stages of the conjugation process. In a period of enabling the at least one kind of reaction fluid to continuously flow through the flow reactor(s), a conjugation reaction is conducted between the first moiety and the second moiety under catalysis of the ligase to produce the conjugate.

Containment and facility systems for offshore porous floating bioreactors that contain algae water slurries in saltwater environments. A containment system may include a containment boom system, a containment silt curtain system, a containment marineworks system, or a combination thereof. Facility systems include an offshore porous floating bioreactor in fluid communication with at least an onshore algae harvesting system. Algae cultivation may occur at an onshore algae cultivation system or within a porous floating bioreactor, and algae lipid production occurs within a porous floating bioreactor. The lipid induced algae is received by the onshore algae harvesting system for further processing.

A Disposable Bioprocess System including a Single-Use-Bioreactor, a Single-Use-Pump and a single-use micro-organism retention filter. Combined most suitable for cultivation of suspended micro-organisms in a liquid media at high micro-organism concentration in a perfusion mode continuous process for expression of biological material. The inlet port of the liquid Single-Use-Pump connects via a valve to the broth reservoir of the Single-Use-Bioreactor through a liquid conveying port. The outlet port of the liquid pumping Single-Use-Pump connects via a valve to a micro-organism retention filter. And a method for operating said sterile Disposable Bioprocess System in perfusion mode for continuously processing.

The disclosure relates to bioreactors, for example for biological treatment and, more specifically to bioreactor insert apparatus including biofilms and related methods. The bioreactor insert apparatus provides a means for circulation of reaction medium within the bioreactor, a biofilm support, and biological treatment of an inlet feed to the reactor/insert apparatus. The bioreactor insert apparatus has a high relative surface area for biofilm attachment and is capable of generating complex flow patterns and increasing treatment efficiency/biological conversion activity in a biologically-active reactor. The high surface area structure incorporates multiple biofilm support structures such as meshes at inlet and outlet portions of the structure. The biofilm support structures and biofilms thereon can increase overall reaction rate of the bioreactor and/or perform some solid/liquid separation in the treatment of the wastewater or other influent.

Herein is reported a feed mixing device for adding feed solutions with a non-physiologically pH value to a cell cultivation vessel comprising a chamber for mixing the feed solutions prior to their addition to the cell cultivation vessel as well as its use. With the feed mixing device as reported herein feed components can be provided in solution at a pH value at which they have good solubility and/or good stability whereby the pH value can be clearly different from the pH value of the cultivation medium, i.e. different from the physiological pH value. This allows performing the cultivation with more flexibility compared to a cultivation in which the pH value of the feed solution is limited to a small range around the pH value of the cultivation.

A bioreactor system is provided that includes a cell culture vessel having a first end, a second end, and at least one reservoir between the first and second ends; and a cell culture matrix disposed in the at least one reservoir. The cell culture matrix has a structurally defined substrate with a surface for adhering cells thereto. The bioreactor system flows material through the at least one reservoir and through the cell culture matrix in a flow direction from the first end to the second end, and the cell culture matrix exhibits isotropic fluid flow permeability therethrough.

The invention provides a process for producing a fermentable gas stream from a gas source that contains one or more constituent which may be harmful to the fermentation process. To produce the fermentable gas stream, the gas stream is passed through a specifically ordered series of removal modules. The removal modules remove and/or convert various constituents found in the gas stream which may have harmful effects on downstream removal modules and/or inhibitory effects on downstream gas fermenting microorganisms. At least a portion of the fermentable gas stream is preferably capable of being passed to a bioreactor, which contains gas fermenting microorganisms, without inhibiting the fermentation process.

A bioprocess system and a method for incubating, growing and harvesting cell cultures is described. Also disclosed is a bioprocess container that can be used with the system. In one aspect of the present disclosure, the bioprocess system includes bioprocess tubes and cell culture tubes having particular dimensions and being made from specific materials that allow the tubes to be welded together while preventing open connections and/or ruptures. In this manner, bioprocess containers can be connected and disconnected from a cell culture apparatus without having to perform the manipulation within a closed environment and without associated monitoring.

Embodiments described herein generally provide for expanding cells in a cell expansion system. The cells may be grown in a bioreactor, and the cells may be activated by an activator (e.g., a soluble activator complex). Nutrient and gas exchange capabilities of a closed, automated cell expansion system may allow cells to be seeded at reduced cell seeding densities, for example. Parameters of the cell growth environment may be manipulated to load the cells into a particular position in the bioreactor for the efficient exchange of nutrients and gases. System parameters may be adjusted to shear any cell colonies that may form during the expansion phase. Metabolic concentrations may be controlled to improve cell growth and viability. Cell residence in the bioreactor may be controlled. In embodiments, the cells may include T cells. In further embodiments, the cells may include T cell subpopulations, including regulatory T cells (Tregs), for example.

The present application provides a pluripotent stem cell-derived neuronal culture system for use in modeling neurodegenerative diseases, drug screening and target discovery; and methods of generating homogenous, terminally differentiated neuronal culture from pluripotent stem cells, and compositions resulting thereof; as well as automated cell culture systems that sustain long-term differentiation, maturation and/or growth of neuronal cells for use in modeling neurodegenerative diseases.