A method for biogas production includes feeding a receiving structure with a feed containing biomass that comprises lignocellulose and directing the feed from the receiving structure into an anaerobic secretome bioreactor (ASB) reactor environment which includes a synthetic microbial community consisting of at least one selected from extremophile thermophilic anaerobic microorganisms that are essentially acidogens and acetogens, the synthetic microbial community producing a secretome of exozymes. The ASB treated biomass is further directed to an aerobic digestion (AD) reactor environment, the ASB treated biomass being pasteurized so as to be essentially free of non-thermophilic microorganisms, the ASB treated biomass comprising liquid effluent containing solubilized biomass products and metabolized biomass products, and solid effluent. Contents or heat are recycled through a conduit between the ASB reactor environment and the AD reactor environment.

A method of installing a flexible bioprocess container in a bioprocessing system having a rigid housing with an interior compartment and extending between a top and an opposing base. The method includes coupling a first surface of the flexible bioprocess container to a moveable platform positioned within the interior compartment of the rigid housing; coupling a second surface of the flexible bioprocess container to the base of the rigid housing; and moving the movable platform relative to the rigid housing and toward the top of the rigid housing so as to at least partially expand the flexible bioprocess container within the interior compartment of the rigid housing.

The present set of embodiments relate to a bioproduction system, method, and apparatus for mixing a fluid. The bioproduction mixing system includes an offset helical assembly having a stabilizer and impeller for mixing a fluid within a flexible compartment The bioproduction mixing system is designed for efficient mixing of the fluid and for use with a variety of different impellers that can be located at different locations according to the volume and shape characteristics of the flexible compartment. The bioproduction mixing system is optimized to eliminate stagnation zones while maximizing bulk fluid flow.

The present set of embodiments relate a system, method, and various devices for installation of a bioproduction system. The bioproduction system includes a rigid housing having a moveable platform to assist in the installation of a bioprocessing container within. The system also includes mounting systems for a variety of peripherals originating from the flexible container while safeguarding operators. More specifically, the system includes systems and methods for mounting bearings, organizing tube sets, and placement of the flexible container in its proper orientation.

Disclosed is an impeller for mixing a fluid wherein the impeller is fashioned so as to substantially reduce areas of fluid acceleration and deceleration around a hub region of the impeller during fluid mixing. Additionally, a bioreactor system having microcarriers, kit of parts and cell culturing method are also provided. The impeller has a generally circularly shaped hub having a downwardly directed progressively tapered volume which has plurality of periods formed therein corresponding to the number of increasingly arced blades. Each of the increasingly arced blades flare outwards to a distal end region of the impeller and have an increasing radius to said arc towards a peripheral edge region of said hub. The flare to the increasingly arced blades defines a larger circumference than that of said hub, thereby imparting a generally frusto-conical shape to the impeller. A method mixing a fluid using the impeller disclosed herein is also disclosed.

Systems and methods for scalable manufacturing of therapeutic cells in bioreactors are disclosed. Fluid dynamic considerations for scale in accordance with an implementation include a method of production of therapeutic cells grown on microcarriers or as cell aggregates in a suspension-based bioreactor includes depositing a suspension comprising cells suspended in a volume of culture fluid into a bioreactor and setting an agitation rate of a mixer disposed in the bioreactor. The method includes actuating the mixer at the set agitation rate to mix the suspension in the bioreactor. The suspension includes a plurality of turbulent eddies generated by the mixer. A magnitude of an energy dissipation rate (EDR) of at least approximately 60% of the turbulent eddies can be less than approximately 0.0015 m2/s3.

Systems for culturing mixotrophic microorganisms on a large scale in thermally stable open systems are disclosed. Embodiments of the system include features such as lit portions, dark portions, organic carbon delivery systems, gas delivery systems, submersible thrusters for mixing, and turning vanes for guiding fluid flow. Multi-functional embodiments of the turning vane provide guidance for fluid flow and other functions such as heat exchange, nutrient delivery, gas delivery, organic carbon delivery, delivery of light, and parameter measurement by sensors.

A facility for the recycling of biomaterial with a fermentation stage, whereby the fermentation stage has a fermentation chamber for the production of biogas through anaerobic fermentation of the biomaterial, and with a hygiene stage that is positioned downstream from the fermentation stage, whereby the hygiene stage has a hygienization chamber for the reception and the thermal hygienization of biomaterial discharged from the fermentation stage. A process for the recycling of biomaterial by zymosis is also provided, whereby biogas is produced in a fermentation stage through anaerobic fermentation of the biomaterial, whereby the biomaterial is, after flowing through the fermentation stage, conveyed to a hygiene stage in which the biomaterial thermal is hygienized, and whereby the biomaterial is, after flowing through the hygiene stage, made available as recyclable agricultural, hygienized fermentation residue.

A wood chip fermentation device includes: a chip fermenter 11 that is charged with wood chips serving as a heat source and that ferments the wood chips; a temperature sensor 11a that is provided inside the chip fermenter 11 and measures the temperature inside the chip fermenter; a thermal energy extracting pipe 12 that is disposed inside the chip fermenter and extracts fermentation heat from inside the chip fermenter; a pump section 13 that supplies a medium to or takes out a medium from the thermal energy extracting pipe 12; a stirring blade 14a that stirs wood chips 10a put in the chip fermenter 11; and a discharge conveyor 15 that is disposed at a lower portion of the chip fermenter 11 and discharges fermented material. The stirring blade 14a is disposed between the thermal energy extracting pipes 12 and a rotating surface thereof is in a state of being parallel to the thermal energy extracting pipes 12. A bottom surface of the chip fermenter 11 is formed in an arcuate shape such as to follow the rotating outer peripheral surface of the stirring blade 14a. A plurality of temperature sensors 11a are installed in a vertical direction inside each chip fermenter. Control of an on-off valve of the thermal energy extracting pipe 12 is performed based on temperature information from the temperature sensors 11a.

A system includes a photobioreactor that provides a channel configured to contain an algae slurry, a duct positioned adjacent the channel and configured to convey a gas, and a barrier separating the duct from the channel and providing one or more apertures to allow a portion of the gas to be injected into the algae slurry from the duct.