A PC comprises a measurement unit, a consumption rate calculation unit, a culture medium replacement detection unit, and a next step transition determination unit. The measurement unit acquires the amount of consumed glucose from the result of continuously measuring the concentration of glucose contained in a culture medium (X) of a culture vessel. The consumption rate calculation unit calculates the consumption rate at which glucose is consumed by differentiating the amount of glucose consumed. The culture medium replacement detection unit detects that the culture medium (X) in the culture vessel has been replaced or added. When the culture medium (X) is replaced or added, the next step transition determination unit determines whether or not to proceed to the next step according to whether or not the consumption rate after the replacement or addition of the culture medium (X) calculated by the consumption rate calculation unit satisfies a specific condition.

The apparatuses described herein relate to preparation of a meat product. Apparatuses, systems comprising the apparatuses, and methods of making and use the systems and apparatuses are described herein. These are useful for controlling one or more of growth on and separation of a meat product from an enclosed substrate. The apparatuses and systems are configured to receive fluid and grow the meat product and/or separate the meat product from the substrate in a scalable manner.

Various embodiments relate to an aeration device for a bioprocessing installation, in particular a bioreactor, comprising a housing, wherein the housing comprises one or more aeration channels in its interior, wherein the housing further comprises one or more gas inlet ports, via each of which a gas can be introduced into at least one aeration channel of the housing, and wherein the housing further comprises a plurality of gas outlet ports, via each of which the gas can be discharged from the respective aeration channel to the outside of the aeration device. It is proposed that the aeration device is configurable with respect to a predetermined discharge of gas via the gas outlet ports.

This disclosure describes a biochemical reactor with a lower divider support structure. The biochemical reactor may include a tank configured to house immobilized carriers and fluid. The biochemical reactor may include a circulation conduit at least partially disposed within the tank. The circulation conduit may include a circulation outlet opening. The biochemical reactor may include one or more vanes disposed proximate to the circulation outlet opening. The biochemical reactor may include a tank recirculation port disposed proximate to a second end. The biochemical reactor may include a tank inlet configured for feeding fluid into the tank. The biochemical reactor may include a tank outlet configured for drawing fluid from the tank. The tank outlet may be disposed proximate to a first end. The biochemical reactor may include a first divider and a second divider. The second divider may include a support structure including a grating configured to withstand variable loads.

Reactor for enzymatic hydrolysis of a raw material comprising in sequence: i)—a first heat exchanger adapted to heat the raw material supplied to the reactor to a temperature within a range that favours enzymatic hydrolysis, ii)—a reactor comprising plural in reactor chambers connected in series, separated by closable valves, iii)—a second heat exchanger adapted to heat the reaction mixture to a temperature higher than the temperature range favouring enzymatic hydrolysis, the reactor being formed with inclined tubular reactor chambers assembled to form a reactor with vertical axis, the first reactor chamber being the vertically uppermost chamber of the reactor, while at least one reactor chamber is adapted to be stirred with a through-flowing inert gas.

A fermenter can have at least one hollow fluid conduit disposed at least partially within a vessel. An external circumference of the hollow fluid conduit and an interior circumference of the vessel can define a downward flow path through which a multi-phase mixture including a liquid media and compressed gas substrate bubbles flows. An interior circumference of the hollow fluid conduit can defined an upward flow path which is in fluid communication with the downward flow path. The multi-phase liquid can flow through the upward flow path and exit the fermenter. Cooling may be provided in the hollow fluid conduit or the vessel. One or more backpressor generators can be used to maintain a backpressure on the fermenter. One or more fluid movers can be used to variously create an induced and/or forced flow in the downward and upward flow paths.

A bioreactor can include a plurality of unit cells. Each unit cell can include a floor configured to support a volume of liquid, the floor being symmetric across at least one axis of symmetry, and an injection port oriented at a center point of at least one axis of symmetry and configured to inject a fluid into the volume of liquid. The bioreactor can also include a peripheral side wall surrounding the plurality of unit cells such that the volume of liquid is retained in the bioreactor.

An exemplary embodiment of the present invention provides an apparatus for producing fermented soybean meal, which produces fermented soybean meal for monogastric animals and ruminant selectively or together. An apparatus for producing fermented soybean meal according to an exemplary embodiment of the present invention includes: a solid-liquid separating part, which mixes raw material soybean meal and an extraction solvent and extracts the soybean meal, and separately produces a remaining soybean meal and a soybean meal extract; a lactic acid bacteria culturing part, which produces the lactic acid bacteria by putting inoculum into the soybean meal extract, and supplies the lactic acid bacteria to the solid-liquid separating part; a solid substrate fermenting part, which is selectively supplied with and mixes at least two of the remaining soybean meal supplied from the solid-liquid separating part, the raw material soybean meal supplied through bypass, and lactic acid bacteria supplied from the lactic acid bacteria culturing part to produce a mixed material, and solid-substrate ferments the mixed material to produce primary solid substrate fermented soybean meal; and a drier, which dries the primary solid substrate fermented soybean meal supplied from the solid substrate fermenting part to produce secondary solid substrate fermented soybean meal.

Autotrophic algal growth in high incident light situations may be conducted in a reactor with circulation of algal reaction medium between light and dark zones with very short residence time in the light zone to maintain algal growth in the reactor in a linear growth regime in which the rate of algal biomass production is proportional to the incident photosynthetic photon flux density. Process monitoring and control may permit quick processing in a single step even in open pond systems. Dissolved nitrogen levels in product may be monitored and nitrogen nutrient input may be restricted to reduce dissolved nitrogen in effluent and to increase lipid yield without a separate nitrogen starvation step.

Described is a method for the culture of microalgae, comprising: providing a consortium of at least two living species of microalgae; culturing under illumination the consortium in a controllable bioreactor and under non-sterile aqueous culture conditions; and controlling the culture conditions for affecting at least one of the following output: (i) flocculation and/or settling of said consortium of microalgae; and (ii) adhesion of the microalgae to surfaces of the bioreactor; wherein said culture conditions are controlled to promote (i) and/or to minimize (ii), without adversely affecting growth of the consortium of microalgae. It is also possible to control the culture conditions for affecting iii) the protein, carbohydrate, and/or fat content of the said microalgae consortium. A system for carrying out the method is also described.