A system for oxygenating a biological culture includes a container bounding a compartment and having a top wall, a bottom wall, and an encircling sidewall extending therebetween; a tubular member projecting into the compartment of the container and terminating at a terminal end; a gas supply coupled with the tubular member and being configured to blow gas through the tubular member; and a mixing element disposed within compartment of the container at a location between the terminal end of the tubular member and the bottom wall of the container, the mixing element being configured to mix the liquid.

The invention relates to a method and to a device for feeding gases or gas mixtures into a liquid, suspension, or emulsion in a reactor in a specific manner. According to the invention, gases or gas mixtures are fed into a liquid, suspension, or emulsion in a reactor in a specific manner, wherein the gas or gas mixture is fed in a specific amount and/or at defined points in time in one pulse as a gas bubble into a flowing liquid in a tilted reactor system, whereby a pulsation effect is obtained, wherein a driving force is produced by means of an adiabatic relaxation of the fed-in gas or gas mixture, by means of which driving force wall adhesions on the reactor are prevented.

Provided is a method for facilitating an aerobic fermentation reaction using combustion waste gas, wherein organic waste in a reactor is heated using waste gas with heat produced from fuel combustion to facilitate the fermentation reaction, some of the chemical substances in the waste gas with heat produced from fuel combustion are absorbed by the organic waste in the reactor, and an environmental friendly treatment is performed on the waste gas with heat produced from fuel combustion. The specific practices comprise: connecting a gas outlet of a combustion device to a conveying pipe, and then connecting the conveying pipe to a gas inlet of the reactor or an air chamber aeration nozzle at a lower part of the reactor. Not only the equipment and cost for combustion waste gas treatments are saved, but also the aerobic fermentation efficiency of the organic waste is improved, which reduces the fermentation time. Not only the combustion waste gas is treated for environmental protection, but also the environmental friendly treatments of organic refuse waste are facilitated; and thus the method is an energy saving and environmental friendly technique.

A bioreactor for cell culture comprising, a first set of open top troughs that are interconnected by a first set off low channels to form a first cascade, a second set of open top troughs that are interconnected by a second set of flow channels to form a second cascade, and a set of interconnecting flow channels coupled between the first cascade and the second cascade, wherein the first cascade circulates a fresh media and the second cascade circulates a cell culture and a first quantity of the fresh media from first cascade is supplied to the second cascade through the set of interconnecting flow channels when a second quantity of cell culture is removed from the second cascade.

A container system includes a flexible bag bounding a chamber. A probe port includes an elongated tubular member having an interior surface bounding a first passageway and extending between a first end and an opposing second end, the first passageway being closed at the first end and open at the second end; and a flange encircling and radially outwardly projecting from the tubular member at or toward the second end thereof, the flange being secured to the flexible bag so that the first end of the elongated tubular member projects into the chamber of the flexible bag while the open second end of the elongated tubular member is accessible from outside of the flexible bag. A probe is received within the first passageway of the probe port.

A bioreactor is provided that includes a main reactor having a configuration selected from the group consisting of stirred and unstirred tank reactor, trickle bed reactor (TBR), cocurrent contactor (CCC), moving bed bioreactor (MBBR), and a bubble column reactor. The bioreactor also includes a growth reactor continuous with the main reactor and having a configuration selected from the group consisting of stirred and unstirred tank reactor, trickle bed reactor (TBR), cocurrent contactor (CCC), moving bed bioreactor (MBBR), and a bubble column reactor. A method is also provided where acetogenic bacteria are contacted with syngas in a growth fermentor section of a reactor vessel that is continuous with a main fermentor section of a reactor vessel.

Provided herein are a device and a method for preparation of immobilized proteins, enzymes or cells on a carrier to achieve the industrial batch production of the immobilized proteins, enzymes or cells.

A mixing bag for use in bioprocessing in which a fluid is received and agitated using an internal fluid-agitating element driven by an external motive device is disclosed. The bag may include an integral sparger and sensor receiver. Related methods are also disclosed.

Provided herein are a device and a method for preparation of immobilized proteins, enzymes or cells on a carrier to achieve the industrial batch production of the immobilized proteins, enzymes or cells.

The invention relates to a novel plasma induced mutation breeding device which comprises: a sample treatment system including a sterile working compartment free of bioactive contaminant; a plasma generator; a radio frequency (RF) power module connected with the plasma generator; a cooling system for cooling the plasma generator; a detection system including a gas flow controller for controlling the gas flow which generates the plasma jet and a temperature sensor for detecting the temperature of the jet emitted by the plasma generator; and a control system with an operation panel and a controller for controlling the operation of the mutation breeding device, wherein the controller is connected with the RF power module, gas flow controller, temperature sensor, cooling system as well as the operation panel, respectively, and said plasma generator stably emits the plasma jet at 37±3° C. during the biological sample processing.