Patent classifications
C12M29/16
POWER DEVICE OF A MICRO CHANNEL FOR EXTERNAL CIRCULATION OF A BIOREACTOR
The present disclosure provides a power device of a micro channel for external circulation of a bioreactor. The power device of the micro channel may be disposed outside the bioreactor and in fluid connection with the bioreactor, the power device of the micro channel may be of a shape of a box body. The power device of the micro channel may comprise: a stacked layer disposed in the box body, including a first shell plate, a second shell plate, and a sealing film sandwiched between the first shell plate and the second shell plate; and a liquid buffer device including a first liquid cavity and a second liquid cavity disposed in the box body, the first liquid cavity and the second liquid cavity may be fixed to an outer end surface of the stacked layer. The power device of the micro channel may be of a box shape, thereby reducing the volume and production cost thereof.
ENCLOSED FILTRATION AND BIOREACTOR SYSTEMS AND PROCESSES
A product concentration device that utilizes a reservoir connected to a hollow-fiber filter element where the reservoir can serve as a container for filtrate emanating from another filtering device, such that product in the reservoir can be stored, concentrated and/or further processed as desired. Enclosed reactor systems, each of at least three chambers, fluid flow between the chambers controlled by selectively permeable barriers, flow controlled by an alternating flow diaphragm pump.
Bioreactor with multiple coupled vessels
A bioreactor system may include (a) two or more fluidically coupled vessels configured to collectively carry out a bioreaction; (b) one or more fluidic paths coupling the two or more vessels to one another, where the fluidic paths are configured to provide flow of culture medium between the two or more vessels; (c) one or more fluid transfer devices along at least some of the one or more fluidic paths; and (d) a control system. The control system may be configured to (i) read or receive values of one or more parameters characterizing the culture medium in one or more of the vessels, and (ii) use the values to determine an adjusted flow rate in at least one of the fluidic paths to maintain substantially uniform values of the one or more parameters in the culture medium from vessel-to-vessel among the two or more vessels.
Disposable alternating tangential flow filtration units
Disclosed herein are robust disposable alternating tangential flow (ATF) housing and diaphragm pump units and associated methods of manufacturing, testing, wetting, and using the same.
Incubated platelet concentration module and method for producing platelet preparation using same
The present invention provides a hollow fiber membrane module which makes it possible to concentrate incubated platelets by efficiently removing water from an incubated platelet suspension liquid containing incubated platelets while suppressing deterioration of the function of the incubated platelets. The present invention provides an incubated platelet concentration module in which a plurality of hollow fiber membranes each having pores with an average pore diameter of 2 μm or less on a surface of the hollow fiber membrane are packed in a casing having at least one inlet for supplying an incubated platelet suspension liquid before concentration into the hollow fiber membranes, wherein a value (X/Y1) obtained by dividing a total cross-sectional area (X) of the plurality of hollow fiber membranes by a total cross-sectional area (Y1) of the least one inlet is 4.0 or less.
Coating a bioreactor
Embodiments provide for introducing a first fluid into a bioreactor and while introducing the first fluid into the bioreactor, circulating a second fluid with a reagent at a first flow rate through the bioreactor. The bioreactor may be maintained in a first orientation for a first period of time to allow at least a first portion of the reagent to coat the bioreactor. The second fluid may then be circulated at a second flow rate slower than the first flow rate to allow a second portion of the reagent to coat the bioreactor. Introduction of the first fluid may promote coating of the bioreactor by ultrafiltration. The introduction of the first fluid may be stopped. A third fluid may be circulated through the bioreactor to remove a portion of the reagent not coated on the bioreactor.
Cell enclosure device and use for same
A cell enclosure device according to the present invention is a cell enclosure device for constructing a multicellular structure obtained by culturing cells, including a porous membrane in at least a portion of the cell enclosure device. In the present invention, a tissue-type chip includes the cell enclosure device in which one type of cells is enclosed. In the present invention, an organ-type chip includes the cell enclosure device in which at least two types of cells are enclosed. In the present invention, a kit for providing a multicellular structure includes an openable and closable sealed container including the tissue-type chip or the organ-type chip and a culture medium. In the present invention, an organ-type chip system includes at least two of the tissue-type chip or the organ-type chip, and the tissue-type chips or the organ-type chips are connected while maintaining a cell enclosure property. A method for culturing cells according to the present invention uses the cell enclosure device.
Filter unit for filtering and method for collecting cells in a liquid cell culture medium
A liquid cell culture medium collecting filter unit includes a porous metal membrane that filters out cells in a liquid cell culture medium, a support that holds a peripheral portion of the porous metal membrane. and a tubular member that has a hollow part serving a flow path for a liquid cell culture medium. The tubular member is connected to the support such that the flow path faces at least part of a main surface of the porous metal membrane.
INTEGRATED ALGAL AND CYANOBACTERIAL PROCESS FOR BIOPRODUCT MANUFACTURING
A bioproduct manufacturing system is disclosed. The system comprises a hollow-fiber primary membrane gas absorber comprising a shell side and a lumen, wherein the primary membrane gas absorber is configured to receive a carbonate salt-based solvent on the shell side and a gas mixture comprising oxygen, nitrogen, and carbon dioxide in the lumen, at least one runway algal cassette reactor-photobioreactor, and a growth medium circulating between the primary membrane gas absorber and the at least one runway algal cassette reactor-photobioreactor. The at least one runway algal cassette reactor-photobioreactor comprises at least one growth chamber coupled to and in fluid communication with a headspace channel so as to define and interior volume, a first condenser coupled to and in fluid communication with the headspace channel, and a harvest line in fluid communication with the at least one growth chamber and coupled to a filter.
CELL CULTURE BIOREACTOR WITH ZONE CONTROL
A cell culture bioreactor has membranes divided into a plurality of zones. The membranes may include perfusion membranes carrying a liquid media and/or gas transfer membranes. The bioreactor has one or more sensors configured to collect data from one or more locations within the bioreactor. The supply of one or more of the gaseous and/or liquid media to a selected zone or zones may be controlled. In some examples, the supply includes a background supply and a selectable incremental supply. The bioreactor may be used to grow cells in suspension. Liquid media circulates within an extra-capillary space of the bioreactor. In some examples, a portion of cells is permitted for a period of time to be restrained within one or more zones of the membranes. Elements of a reactor may be made in a mold. A reactor may be operated in a fed-batch process.