Processes, methods, and apparatus for carbon sequestration utilizing catalysis schemes configured to provide high concentrations of hydrated CO.sub.2 in proximity with a sequestration agent are provided. Reactants are combined with catalyst such that at least two regions of controlled catalytic activity form encompassing at least the interface between a sequestration agent and an aqueous solution containing dissolved CO.sub.2. Suitable reactants include various sequestration agents, catalyst, and carbon dioxide dissolved in an aqueous solution (seawater, for example). Possible products include bicarbonate and metal cations.

At least one elongated photobioreactor, at a small angle relative to horizontal and mixed substantially or entirely by large bubble flow, is used for contained cell culture, e.g., microalgae cultivation. Elongated, flexible, transparent, polymeric photobioreactor tubes, in near-grade and near-horizontal (e.g. sloped 1 degree to 3 degrees) orientation, and use of low-pressure air mixing, allow very inexpensive construction and operation. Multiple elongated tubes may be used for an independent operation of the multiple photobioreactor tubes for the same or different cells, e.g., microalgae and different applications. Low-pressure air is delivered near the low end of the bioreactor at less than 10 psig and without sparging, to produce large air bubbles that travel from the low end to the high end of the bioreactor, for turbulent mixing and gas exchange. Each inexpensive, flexible bioreactor tube is easily modified to improve internal flow characteristics and suspension of cells, and/or to include sensor and/or sampling collars and ports.

A micro-fluidic system for a perfusion cell culture is disclosed. The system includes: a substrate; a micro-fluid injection channel defined in the substrate to guide fluid in a plane direction of the substrate; at least two micro-fluid branch channels defined in the substrate, wherein the branch channels are branched from the micro-fluid injection channel; micro-fluid outlet channels defined in the substrate, wherein each of the outlet channels extends from a distal end of each branch channel to a top face of the substrate, wherein each outlet channel has each through-hole defined in the top face portion of the substrate; and well plates disposed on the top face of the substrate, wherein each of the well plates fluid-communicates with each outlet channel. The micro-fluidic system refers to a technique that adjusts a flow of liquid or gas of a very small amount (nanoliter or picoliter) in an extremely miniaturized device.

A cell culture device includes a storage tank having one or a plurality of cell culture units. Each of the cell culture units includes a first liquid storage chamber having an airtight structure in which a liquid is to be stored, a second liquid storage chamber in which the liquid is to be stored, a culture liquid storage chamber having a culture liquid storage space in which a culture liquid of cells is to be stored, a permeable membrane having one surface to which the cells are able to adhere, said one face facing the culture liquid storage space, and a liquid lead-out flow path that introducing the liquid from a space on the other surface side of the membrane into the second liquid storage chamber, the first liquid storage chamber being set as a supply source of the liquid.

Under one aspect, a fermentation system includes a fermentation vessel having a straight wall length L and an inner diameter D. The fermentation system also can include a source of a gas including a reactive gaseous component. The fermentation system also can include spargers spaced apart from one another along the straight wall length L of the fermentation vessel and configured to introduce bubbles of the gas into fermentation broth within the fermentation vessel. The release of the bubbles of the gas by each of the spargers can establish a respective mixing zone within the fermentation broth within the fermentation vessel. Each mixing zone can have substantially the same volumetric uptake rate of the reactive gaseous component by the fermentation broth as each other mixing zone.

A cell culture device includes plural three or more of culture vessels, a flow path that connects the plural culture vessels to each other, and a transfer control unit that performs transfer control to transfer a cell suspension housed in any of the plural culture vessels to any other of the plural culture vessels via the flow path.

Embodiments disclosed herein relate to novel flasks, methods and systems employing said novel flasks, and sensors for use within said flasks and systems. In some embodiments, flasks and systems described herein are used to culture cells and/or detect changes in pH levels or dissolved oxygen and/or carbon dioxide levels in a cell culture sample resulting from the growth of living cells contained within a reaction vessel such as a flask. The devices may be used to detect changes in pH and dissolved oxygen levels in a liquid contained in the reaction vessel due to growth of living cells.

A system for growing algae includes a photobioreactor comprising a tubular structure having inner and outer surfaces, an annular space defined between the inner and outer surfaces, an inlet to allow an algae slurry to enter the annular space, and a mechanism configured to produce radially-directed contractions and expansions in the tubular structure. At least one of the inner and outer surfaces is transparent to at least some wavelengths of light useful for growing algae within the algae slurry.

The present invention provides for a fully integrated microfluidic system capable of producing single-dose amounts of biotherapeutics at the point-of-care wherein protein production, purification and product harvest are all integrated as a single microfluidic device which is portable and capable of continuous-flow production of biotherapeutics at the microscale using a cell-free reaction system.

A cell culture bioreactor has perfusion membranes and gas transfer membranes or a gas phase in an extra-membrane space in contact with a film on the perfusion membranes. Gas transfer membranes may travel through the perfusion membranes or through the extra-membrane space. Examples with hollow fiber and flat sheet membranes are shown. One or more of the membranes optionally has a responsive surface, for example a thermo-responsive surface. In some examples, membranes are located in X-Y planes while the length of the reactor extends in a Z-direction.