This disclosure describes a biochemical reactor with a lower divider support structure. The biochemical reactor may include a tank configured to house immobilized carriers and fluid. The biochemical reactor may include a circulation conduit at least partially disposed within the tank. The circulation conduit may include a circulation outlet opening. The biochemical reactor may include one or more vanes disposed proximate to the circulation outlet opening. The biochemical reactor may include a tank recirculation port disposed proximate to a second end. The biochemical reactor may include a tank inlet configured for feeding fluid into the tank. The biochemical reactor may include a tank outlet configured for drawing fluid from the tank. The tank outlet may be disposed proximate to a first end. The biochemical reactor may include a first divider and a second divider. The second divider may include a support structure including a grating configured to withstand variable loads.

The present invention relates to methods and apparatus for microbial conversion of carbon dioxide, carbon monoxide and hydrogen to methane, and to the microbial populations, and the media comprising the microbial populations, that may be used in such methods and apparatus.

A method for automated processing of a cellular product comprising target substrate cells, the method comprising providing a separation apparatus configured to associate with a disposable sterile circuit comprising a separator in communication with the cellular product. The apparatus and disposable sterile circuit are configured to remove platelets from the cellular product to form a platelet-depleted cellular product, resuspend the platelet-depleted cellular product in media to form a resuspended platelet-depleted cellular product, receive an agent having an association with the target substrate cells of the resuspended platelet-depleted cellular product, incubate the agent with the target substrate cells over a period sufficient for the agent to bind with and/or enter the target substrate cells to form a first mixture comprising agent-target substrate cell complexes, unbound/unassociated agent, and non-target substrate cells, and remove unbound/unassociated agent to form a second mixture comprising the agent-target substrate cell complexes and non-target substrate cells.

An incubator 1 includes a cultivating chamber 4 for cultivating culture in a plurality of containers 3 and a supply device 5 provided outside the cultivating chamber 4 and supplying steam into the cultivating chamber 4 for humidification. The supply device 5 includes a supply chamber 5A in which a tray 42 for reserving water is accommodated and an ultrasonic atomizing device 43 for atomizing water. The water in the tray 42 is easily made into steam by the ultrasonic atomizing device 43, passes through an HEPA filter 45 provided in an opening portion 5B and is supplied into the circulation passage 37 of the cultivating chamber 4.

Gas-utilizing microorganisms are stably cultured regardless of variations in a supply flow rate of a substrate gas. Gas-utilizing microorganisms 9 are cultured in a culture solution 2 in a culture tank 10. A substrate gas containing CO and H.sub.2 or the like is supplied to the culture tank 10 and is dissolved in the culture solution 2. When a supply flow rate of the substrate gas or predetermined constituents of the substrate gas to the culture tank 10 becomes a predetermined value or lower, a culture solution 2a is rapidly discharged from the culture tank 10.

A method for the continuous flow synthesis of (R)-4-halo-3-hydroxy-butyrate using a micro-reaction system. The micro-reaction system includes a micro-mixer, a certain number of micro-reaction units that are successively connected in series, a pH regulating system and a back pressure valve. The micro-reaction unit is composed of a micro-channel reactor and a pH regulator that are sequentially connected with each other. A substrate solution containing halogenated acetoacetate and a biocatalyst solution are simultaneously pumped into the micro-reaction system to enable continuous flow biocatalytic asymmetric reduction reaction of the halogenated acetoacetate to obtain the target product (R)-4-halo-3-hydroxy-butyrate.

A culture container has a first inflow port and a first outflow port. The first flow path connects the first outflow port to the first inflow port. A storage container is provided within the first flow path and has a second inflow port which is connected to the first outflow port and a second outflow port which is connected to the first inflow port. A second flow path connects a first region within the first flow path, and a second region within the first flow path. A division processing portion is provided within the second flow path, performs a division process of dividing a cell aggregation flowing in from the first flow path, and allows the cells subjected to the division process to flow out into the first flow path via the second region. A medium supply portion supplies a medium to the inside of the first flow path.

The present invention is directed to a multi-organ-chip device comprising a base layer; an organ layer arranged on the base layer; an antra layer arranged on the organ layer; and an actuator layer; wherein the base layer is configured to provide a solid support for the further layers; the organ layer is configured to comprise a multiplicity of individual organ equivalents, each organ equivalent comprising one or more organ growth sections, each of the organ growth sections being configured to comprise an organoid cavity for housing at least one organoid of an organ and to comprise a micro-inlet and a micro-outlet for fluid communication between the organoid cavity of the organ growth section and a self-contained circulation system, wherein the organ layer comprises at least one organ equivalent configured to represent the organs lung, small intestine, spleen, pancreas, liver, kidney and bone marrow, respectively, and a self-contained circulation system configured to be in direct fluid communication with the organ growth sections of the organ layer via the micro inlets and outlets of the organ growth sections; the antra layer is configured to comprise a multiplicity of cavities and tubes arranged to be in fluid communication with selected organ equivalents or organ growth sections in order to allow for exchange of fluids between cavities and organ growth sections; and the actuator layer is configured to comprise a multiplicity of actuators arranged and configured to regulate a pressure force applied on a selected organ equivalent, the self-contained circulation system and/or part thereof.

A tissue processing apparatus, a filter and a method for processing tissue therefrom #! The problem to be solved is to provide a portable apparatus for processing harvested fat to form a good quality graft that does not clog syringes, and the problem is solved by providing an apparatus as in the present invention with a filter that is inclined to the base of the apparatus and comprises of plurality of elongated protrusion that are structured at an angle on the surface of the filter and blocks the fibres when the harvested fat moves on the inclined surface of the filter, thereby filtering the harvested fat and avoiding clogging of syringes.

A method for separating a biological suspension includes dispensing a liquid suspension comprised of cells or microorganisms from a bioreactor or fermenter into a sterile compartment of a first bag assembly, the first bag assembly including a collapsible bag having of one or more sheets of flexible film. The compartment of the first bag assembly is sealed closed. The first bag assembly, either with or without a manifold fluid coupled therewith, is then rotated, such as by using a centrifuge, so that the liquid suspension separates within the compartment into a pellet comprised of the cells or microorganisms and a liquid supernatant.