In a first aspect of the present invention, a manipulation method of an organism is provided, comprising: forming an air bubble by introducing gas into liquid in which an organism is submerged; controlling of energy before, during or after the forming of the air bubble, including controlling of difference (E1 - E2) obtained by subtracting, from surface free energy E1 at an interface between the gas and the organism, surface free energy E2 at an interface between the gas and the liquid; and manipulating the organism using the air bubble, by bringing the air bubble into contact with the organism during or after the controlling of energy.

The present invention pertains to methods for manufacturing high titer antibody products. In particular, the invention pertains, in part, to improved serum-free animal cell culture medium, which can used for the production of a protein of interest. Additionally, the present invention further pertains to chromatographic procedures employed to successfully isolate the antibody product subject of the present disclosure.

The present disclosure provides controlled bioprocessing systems for enhanced minicell production with defined fermentation parameters and methods of said bioprocessing systems and methods for the production of minicells from said bioprocessing systems using a bioreactor or fermenter.

The application discloses a uniform material distribution control method and system for fermentation tank in an aerobic fermentation apparatus for organic solid waste. A total amount of materials in the fermentation tank and an average material distribution amount at each material distribution point are acquired; a target speed for material distribution at each material distribution point is determined according to the total amount of materials, the target speed is corrected according to the average material distribution amount and a target average material distribution amount when the average material distribution amount is not equal to the target average material distribution amount, and an advanced announcement time of the target speed is calculated according to the corrected target speed, a distance in the fermentation tank and a closed-loop regulation lag time; a closed-loop control to the total amount of materials is performed based on the advanced announcement time of the target speed.

The present invention pertains to methods for manufacturing high titer antibody products. In particular, the invention pertains, in part, to improved serum-free animal cell culture medium, which can used for the production of a protein of interest. Additionally, the present invention further pertains to chromatographic procedures employed to successfully isolate the antibody product subject of the present disclosure.

The present application relates to biotechnological fluid treating, such as biopharmaceutical liquids in order to obtain products such as monoclonal antibodies, vaccines or recombinant proteins, and particularly to a system for treating a biotechnical fluid, having a bioprocess machine and at least one bioprocess machine helper, configured to connect to each other and each comprising a controller, in turn comprising a machine-to-machine communication tool configured for connecting to a network

Provided are a cell culture apparatus capable of culturing cells with a high yield and time efficiency by efficiently advancing bead to bead transfer of the cells in a case where culture carriers are introduced into a suspension and cells are cultured on the culture carriers, and a method for manufacturing a cell group. A cell culture apparatus includes a culture container that accommodates a suspension containing at least cell complexes that are complexes of cells and culture carriers; a drive device that agitates the suspension; a measurement device that measures at least one of a cell distribution information value related to the cells and a carrier distribution information value related to the culture carriers in at least one partial region in the suspension; and a control device that controls driving of the drive device on the basis of at least one of the cell distribution information value and the carrier distribution information value measured by the measurement device.

A bioreactor for producing hydrogen gas and other metabolites. The bioreactor utilizes light, fermentation, and other metabolic processes for the production of metabolites, derived from various microorganisms contained within the bioreactor through respective metabolic pathways. The bioreactor comprises a main reactor chamber, a semipermeable membrane, a sleeve, a power supply, a substrate medium, a heating member, a plurality of tubing members, a collection reservoir, a pressure-sealed connecter member, and an agitator.

A bioreactor includes a base and a lid. The base includes two opposing curved or convoluted surfaces, two opposing flat surfaces, a window disposed on one of the flat surfaces, the window having a higher degree of transparency compared to other portions of the base, wherein images or videos of cells are captured through the window by non-invasive ISM device, and a rounded bottom. The lid is attachable to the base. The lid includes a shaft and a semipermeable membrane attached to the shaft, the semipermeable membrane being permeable to oxygen but impermeable to viruses and bacteria. The PAT-based online analysis directs the adaptive manipulations of bioreactor towards efficient, automated, and GMP-compliant clinical protocols of cell culture.

A bioreactor including a containment structure containing a liquid culture medium for cultivating seaweed. The containment structure includes a sidewall extending vertically between a top and bottom section where the bottom section has an effluent arranged to allow extraction of cultivated seaweed. A spiral liner is positioned adjacent to an inside surface of the sidewall. The recirculator includes a pump arranged to continuously receive a portion of the liquid culture medium via an inlet from the bottom section and output the liquid culture medium via the outlet at the top section. Sensors monitor environmental conditions within the bioreactor. Light emitters are arranged along a surface of the spiral liner. Flow generators, positioned within the containment structure in a spiral configuration between the top section and bottom section, are configured to direct a flow of the liquid culture medium from the top section toward the bottom section of the containment structure.