The present set of embodiments relate to a bioproduction system, method, and apparatus for creating a scalable bioreactor system. Specifically, the present set of embodiments enable the determination of bioreaction performance characteristics of a commercial scale by matching operational parameters between a small test scale bioreaction to that of a commercial scale bioreaction. The system and methods do not rely on simply making bioreactor apparatuses across scales the same dimensionally which would not account for differences in fluid dynamic properties between very small to very large volumes, but requires tuning of a variety of systems (mixing assembly, sparger system, and headspace airflow system) in conjunction with one another to achieve predictive outcomes.

The present disclosure provides a system, including methods and apparatus, for culturing, monitoring, and/or analyzing organoids. In an exemplary method of organoid culture, the method may comprise disposing a scaffold in a receptacle having an open side. A sealing member may be bonded to the open side of the receptacle to create a chamber. An organoid may be formed in the chamber using the scaffold. Fluid and/or at least one substance may be introduced into the chamber from an overlying reservoir for contact with the organoid.

The invention comprises one or more gas volume fraction measurement devices operatively connected to one or more controllers and one or more deaeration mechanisms which receive control signals from said one or more controllers and perform an act on the system, such as by controlling a level of deaeration chemistry into some portion of the fermentation system. In one embodiment, the deaeration mechanism is an antifoam feed pump which pumps antifoam chemistry into a feed line of the fermenter in response to the measured gas volume fraction in the fermenter's recirculation loop, in an amount determined by the controller to be effective to reduce foaming and lower column height in the fermenter.

A system and method for the production of microbial consortiums and by-product material is provided. A physical containment system comprising phase spaces arranged in a discrete order to favor specific biological reactions is also provided. Phase profiles and phase data sets include the pre-determined physical and biological parameters for the phase space transitions. Movement of material from one phase to the next is hydraulically balanced enabling working fluid to continuously move in a fixed direction and rate of flow. Continuous monitoring of phase profiles and phase data sets provide feedback to the system enabling alteration of the conditions in the system to control reactions therein.

A millifluidic device for cultures of biological agents comprising: a main body (11) comprising at least a first hole (40) closed at the bottom; a separator (35); a membrane (36) fixed to said separator (35); a plug (15) closing said first hole (40); said separator (35) designed to be placed in said first hole (40); said separator (35) being extractable from said first hole (40); said membrane (36) divides said first hole (40 ) into an upper half-chamber and a lower half-chamber; a pair of tubes (25) to perfuse said lower half-chamber; a pair of tubes (26) to perfuse said upper half-chamber; a first slide (22) placed centrally on said plug (15); a second slide (42) placed centrally on said first hole (40); a cylindrical body (41) rises from said first hole (40) and said second slide (42) is placed on the top of said cylindrical body (41); said cylindrical body (41) has a second hole (43), coaxial to said cylindrical body (41).

One aspect of the invention provides a method of generating bacteriophages adapted to infect a target bacterial strain. The method comprises: providing host bacteria that are susceptible to phage as input to a host chemostat containing phage; providing target bacteria that are related to the host bacteria, but not susceptible to phage as input to a target chemostat containing phage; filtering outflows from the host chemostat and the target chemostat to isolate phage from the populations of the host bacteria, the target bacteria, and macromolecules; combining the outflows; and introducing the combined outflow into each of the host chemostat and the target chemostat.

Example embodiments include a cell culture apparatus, methods for cell cultivation by using the cell culture apparatus, and a cell culture incubator comprising the cell culture apparatus. The cell culture apparatus comprises a plurality of cell culture modules arranged adjacent to each other. Each cell culture module comprises two or more culture medium reservoirs connected by two or more flow channels that go through a basal chamber arranged under an apical chamber. The apical and basal chambers are separated by a porous membrane. The basal chamber has a bottom part arranged higher than a bottom part of each of the culture medium reservoirs. The culture model comprises further a cavity under at least the bottom part of the basal chamber and at least one means for capturing at least one image from a bottom and/or top of the at least one cell culture module.

An improved dry grind system and method for producing a sugar stream from grains or similar carbohydrate sources and/or residues, such as for biofuel production. In particular, a sugar/carbohydrate stream, which includes a desired Dextrose Equivalent (DE) where DE describes the degree of conversion of starch to dextrose (aka glucose) and/or has had removed therefrom an undesirable amount of unfermentable components, can be produced after saccharification and prior to fermentation (or other sugar conversion process), with such sugar stream being available for biofuel production, e.g., alcohol production, or other processes. In addition, the systems and methods also can involve the removal of certain grain components, e.g., corn kernel components, including protein, oil and/or fiber, prior to fermentation or other conversion systems. In other words, sugar stream production and/or grain component separation occurs on the front end of the system and method.

A perfusion module and a perfusion culture system are provided, including: a bioreaction module, including at least one bioreactor; a perfusion module, including at least one perfusion chamber, each perfusion chamber is connected to a pressure regulating pipe for inflow or outflow of an airflow; when there are multiple perfusion chambers, every two adjacent perfusion chambers are connected to each other; at least one bioreactor, the perfusion module, the filtration module are communicated in sequence, if there are more than two perfusion chambers, all of perfusion chambers are set side by side; a cell culture fluid in at least one bioreactor flows into at least one perfusion chamber, flows out from at least one perfusion chamber into at least one filter, and a permeate from at least one filter flows into a harvesting device. The present disclosure avoids high shear forces in the perfusion culture system.

Apparatus for purifying a liquid comprising a target substance comprising at least two units arranged in series such that the feed stream of the second and any subsequent units comprises the product stream from a downstream unit, wherein each unit comprises specified components (i) to (vi), including a a switchable bypass assembly. Also claimed are the units and a flowpath assembly. The units may be essentially the same except for a device they contain, leading to advantages in terms of simplicity, cost and ease of operation, lower risk of operator error, easier maintenance and lower inventory of spare parts.