Abstract: A bioprocess system and a method for incubating, growing and harvesting cell cultures is described. Also disclosed is a bioprocess container that can be used with the system. In one aspect of the present disclosure, the bioprocess system includes bioprocess tubes and cell culture tubes having particular dimensions and being made from specific materials that allow the tubes to be welded together while preventing open connections and/or ruptures. In this manner, bioprocess containers can be connected and disconnected from a cell culture apparatus without having to perform the manipulation within a closed environment and without associated monitoring.

Abstract: An inverted conical bioreactor is provided for growing cells or microorganisms. The bioreactor has an internal space and a perforated barrier within the vessel, through which a liquid may flow, where cells or microorganisms cannot pass through the perforated barrier. The perforated barrier divides the internal space of the bioreactor into a first chamber and a second chamber. Cells are grown within the second chamber and can be perfused by re-circulating the liquid, for example a growth medium, through the bioreactor. Various inlet ports and outlet ports allow controlling the parameters of flow of the growth medium.

Abstract: A transfection device suitable for delivery of various macrostructures (e.g., mitochondria, bacteria, liposomes) is described and uses mechanical force to thereby induce active endocytosis in a target cell. Contemplated devices are able to achieve high throughput of transfected cells that remain viable and are capable of producing colonies.

Abstract: Disclosed is a cell culture system comprising a first cell culture bioreactor system (10) for culturing cells to a predetermined cell density or quantity, the system including a bioreactor volume (20), a process controller (30), process control devices (32) which provide inputs (16) for the culture volume and culture parameter measurement devices (14), wherein the process controller is operable according to plural control program steps to control the process devices to provide inputs for a suitable cell culture environment in the bioreactor volume, and is further operable according to control program steps modified by feedback values from the culture parameter measurement devices, and comprises a memory (36) operable to record data indicative of the progress of the control program steps.

Abstract: An active solid state fermentation bioreactor for producing gases, liquid(s) or solids from gaseous or gaseous and liquid starting materials and a fermentation process using the reactor are disclosed, The bioreactor includes three major phases; a solid phase including the porous solid support, a liquid phase comprising liquid, and a gaseous phase. The solid phase includes a porous solid support, in which at least 20% of the pore volumes have a size resulting in a liquid suction of about 0.01 to about 0.1 bars if these pores are filled with liquid, the porous solid support is inoculated with desired micro-organisms, the volume of the gaseous phase is 20% to 60% of the volume of the bioreactor, and the liquid phase is at least 20% of the reactor volume, The unsaturated capillary conductivity of filling/packing solid material of the bioreactor is at least 0.1 cm/ h.

Abstract: A cell capture, disruption, and extraction method includes a introducing a plurality of abrasives in a disruption chamber, which can include diamond powder, variably and multi dimensionally disbursed therein, and a pestle positioned in the disruption chamber. The method includes agitating the abrasives by moving the disruption chamber and/or pestle, agitation of the abrasives tearing cell structure in the solution to access its contents. A binding column or size exclusion column can be positioned downstream of the disruption chamber. Cell solution can first be introduced in the disruption chamber, the abrasives capturing the cells and allowing therethrough and purging the waste content, then breaking the cell content. The lysate can then bind to an extraction matrix downstream of the disruption chamber or it can be mixed in with the abrasives.

Abstract: The invention relates to a bioreactor including: a light source (200); a light sensor (300) facing said light source; a vat (100) that is placed between the light source (200) and the light sensor (300), said vat being intended to receive a culture medium comprising a cellular culture of photosynthetic microorganisms; a controller (400) connected to the light sensor (300) in order to control the vat (100) to obtain a chosen cellular-culture concentration (xi) in the culture medium during a working period, said light source (200) being capable of emitting incident light (L) of an input light intensity (Iin) in the direction of the vat (100), and the light sensor (300) being capable of measuring an output light intensity (Iout) and of transmitting data relating to this intensity (Iout) to the controller for the control of the vat; and a system (500) for controlling the light source (200), this system being arranged to adjust, during a period shorter than or equal to said working period, the input light intensit

Abstract: A reaction processing vessel includes a substrate and a groove-like channel formed on the upper surface of the substrate. The channel includes a high temperature serpiginous channel, a medium temperature serpiginous channel, and a high temperature braking channel and a medium temperature braking channel that are adjacent to the high temperature serpiginous channel and the medium temperature serpiginous channel, respectively. The respective cross-sectional areas of the high temperature braking channel and the medium temperature braking channel are larger than the respective cross-sectional areas of the high temperature serpiginous channel and the medium temperature serpiginous channel, respectively.

Abstract: A sensor device according to the present technology includes a stack sensor. The stack sensor includes a first sensor layer and a second sensor layer. The first sensor layer has, as a detection target, a first substrate in a culture solution, the first substrate being changed in accordance with a change in a state of a cell. The second sensor layer has, as a detection target, a second substrate in the culture solution and is provided on the first sensor layer, the second substrate being changed in accordance with the change in the state.

Abstract: A bioreactor system includes a vessel having a bottom floor, a flexible bioprocessing bag disposed within the vessel, and a flexible bladder positioned intermediate the bottom floor of the vessel and the bioprocessing bag. The flexible bladder is selectively inflatable to vary at least one of a geometry or configuration of the bioprocessing bag to provide for improved drainability or an increased turndown ratio for the bioreactor system.

Abstract: A liquid feed device that feeds a liquid medium and a cell suspension to target containers by respectively suited liquid feed methods is provided. A pump 6 is connected between a first liquid bottle 12 containing a liquid medium and a second liquid bottle 2 containing a cell suspension, and a receptacle 8 to be used as a culture container is connected downstream of a second liquid bottle 12. The liquid medium in the first liquid bottle is sent to the receptacle through the pump 6 and a branch point 20 by opening a first supply valve 17, and the cell suspension in the second liquid bottle is sent to the receptacle by opening a first gas introducing valve 10, a second gas introducing valve 15, and a second supply valve 19 and transferring, by pressure, a gas supplied from the first gas introducing valve 10 to the second liquid bottle through the pump 6 and a branch point 16.

Abstract: The present invention relates to a large-scale photosynthetic bioreactor in which transparent photobioreactors including a baffle are connected in parallel or in series by an adhesive element so that the reactor volume can be easily scaled up for scale-up culture of photosynthetic organisms, and to a fabrication method thereof. The large-scale photosynthetic bioreactor according to the present invention makes it possible to culture a larger amount of microalgae than a conventional photobioreactor in the same area. In addition, it has high light transmittance, produces a large amount of biomass per unit area due to smooth mixing, and has a significant effect of reducing carbon dioxide. Furthermore, the present invention has an advantage in that the number of photosynthetic bioreactors required to culture the same scale of photosynthetic organisms is significantly smaller than that in a conventional process for culture of photosynthetic organisms, and thus the operating costs can be reduced.

Abstract: Embodiments of the invention relate to a Disposable Bioprocess System including a Single-Use-Bioreactor, a Single-Use-Pump and a single-use micro-organism retention filter. Combined most suitable for cultivation of suspended micro-organisms in a liquid media at high micro-organism concentration in a perfusion mode continuous process for expression of biological material. The inlet port of the liquid Single-Use-Pump connects via a valve to the broth reservoir of the Single-Use-Bioreactor through a liquid conveying port. The outlet port of the liquid pumping Single-Use-Pump connects via a valve to a micro-organism retention filter. And a method for operating said sterile Disposable Bioprocess System in perfusion mode for continuously processing.

Abstract: The present invention relates generally to tissue container systems that find use in the transport of tissues and methods of using the tissue container systems. In particular the present invention relates to systems that support the transport, thawing and use of cryopreserved human skin equivalents, and methods of their use by a health care provider.

Abstract: A cell stretching device including a cell chamber having upper and lower portions is disclosed. The lower portion has fixing means for fixing a deformable cell substrate (S) to the cell chamber and defining a stretching region inside the chamber at the lower portion. The upper portion has stretching means movable relative to the chamber and acting on the cell substrate (S) and a support element for holding the stretching means and a driving unit coupled to the upper portion of the cell chamber and engageable to the stretching means for mechanically controlling and regulating the movement of the stretching means relative to the cell chamber. The stretching means include clip members operating inside the stretching region which are configured to clamp the cell substrate (S) at a clamping contact point and to stretch the cell substrate (S) in response to the movement.

Abstract: A method of treating a heavy metal contaminated soil including contacting the contaminated soil with a bioremediation mixture for a predetermined time such that the contaminated soil is anaerobically digested, wherein the contaminated soil contains one or more heavy metals, and wherein the anaerobically digested soil contains a lesser amount of the one or more heavy metals than the contaminated soil.

Abstract: A system for aerobic fermentation includes a vessel, an aeration system including a gas sparger fluidly coupled to the vessel to introduce a compressed gas to an internal volume of the vessel, and a recirculation loop fluidly coupled to an outlet of the vessel. The recirculation loop includes an eductor fluidly coupled to an oxygen-containing gas source, a static mixer downstream of the eductor, a heat exchanger downstream of the eductor, and a distributor downstream of the heat exchanger. The distributor is fluidly coupled to the vessel. The aeration system provides mixing and oxygen mass transfer to the fermentation composition in the vessel. The fermentation composition passes through the eductor, static mixer, heat exchanger, and distributor of the recirculation loop, and back into the vessel. Oxygen is transferred from an oxygen containing gas to the fermentation composition and heat is removed from the fermentation composition in the recirculation loop.

Abstract: The present invention discloses a piezoelectric ultrasonic microinjection device based on a flexible hinge mechanism. The device includes: a cover, a flexible hinge mechanism, a base, a screw cap and an end cap fixedly assembled together, the base being provided with a pump interface; and a micropipette fixedly mounted in the base, the screw cap and the end cap and extending outward, the micropipette being in communication with the pump interface; wherein the flexible hinge mechanism comprises a housing, a piezoelectric ceramic package module encapsulated in the housing, a central shaft fixedly mounted with the piezoelectric ceramic package module and the base, and a vibration output shaft extending from the piezoelectric ceramic package module into the central shaft, a plurality of flexible hinge beams being disposed between the central shaft and the housing.

Abstract: A belt for an algal growth system includes a flexible sheet material configured to facilitate growth of a biofilm. The flexible sheet material is mounted on a first frame in a first mounted geometry, the flexible sheet material having a substantially vertical orientation when mounted on the first frame such that a first height of the first mounted geometry is greater than a first width of the first mounted geometry, the flexible sheet material being in contact with a contacting liquid.

Abstract: Cell culture apparatus for emulating gastrointestinal tract conditions and comprising at least two adjacent, microfluidic, cell cultivation channels separated by a permeable or semipermeable membrane, a first channel carrying gastrointestinal tract epithelial cells or tissues and a second channel carrying luminal and preferably mucosal microbiota, and wherein said second channel comprises one or more dwell chambers capable of providing a location for unattached luminal flora to reside away from any direct flow in said second channel, permits modelling of multiple sections of the gastrointestinal tract and control of retention times.