Culture systems and methods of using same. The systems include a housing defining an inner space. The inner space includes a headspace and at least a portion of a reservoir. A surface for immobilizing cells is moveable between the headspace and the reservoir. The systems can be used for coculturing methanotrophs and phototrophs for processing biogas and wastewater, particularly from anaerobic digesters.

A culture container linkage device according to the present disclosure includes a first actuator configured to advance or retract needles 32, an actuator holder rotatably provided on a frame and configured to hold the first actuator, a second actuator, and a washer configured to wash the needles. The second actuator rotates the needles via the actuator holder. The needles are configured to be positioned, by the second actuator, at a container-facing position at which the needles face a culture container and a washing-facing position at which the needles face the washer.

The microorganism preparation feeding method of the invention employs an automatic microorganism preparation feeding apparatus which includes a cold storage apparatus for refrigeration-storing a seed microorganism belonging to the aerobic microorganism group including at least one species of aerobic microorganisms capable of decomposing oil and fat contained in oil/fat-including wastewater and a growth tank for growing the seed microorganism so as to produce the microorganism preparation, wherein the seed microorganism belonging to the aerobic microorganism group is maintained in a live state by means of the cold storage apparatus, the seed microorganism is periodically grown by means of the growth tank so as to produce a predetermined microorganism preparation, and the produced predetermined microorganism preparation is fed to the oil/fat-including wastewater. The method includes refrigeration-storing, as the seed microorganism, a microorganism whose population density is 1×10.sup.7 CFU/mL to 5×10.sup.9 CFU/mL in the cold storage apparatus; growing, as a source material, the seed microorganism of a predetermined volume by means of the growth tank so as to produce the predetermined microorganism preparation whose volume is 50 to 500 times the predetermined volume of the seed microorganism and whose population density is 1×10.sup.7 CFU/mL to 2×10.sup.10 CFU/mL; and feeding the produced microorganism preparation to the oil/fat-including wastewater.

A conjugation device includes at least one flow reactor having an inlet and an outlet, the flow reactor(s) being completely filled with a support such as a matrix including 1) chromatography beads, fibers or membranes, and 2) a biologic catalyzer, namely the enzyme ligase, which is immobilized onto this support; a fluid delivery unit in fluid communication with the inlet of the flow reactor(s) and configured to continuously provide the flow reactor(s) with at least one kind of reaction fluid such as antibody and linker-payload according to stages of the conjugation process, the at least one kind of process fluid including a first moiety and a second moiety of a conjugate to be produced; and a fluid collection unit in fluid communication with the outlet of the flow reactor(s) and configured to control collection of fluid flowing out of the outlet of the flow reactor(s) according to the stages of the conjugation process. In a period of enabling the at least one kind of reaction fluid to continuously flow through the flow reactor(s), a conjugation reaction is conducted between the first moiety and the second moiety under catalysis of the ligase to produce the conjugate.

A biogas digester tank heating method, system and modular heating rack is provided. The method can include providing a digester tank having a base and a vertical wall surrounding the base. A plurality of heating racks can be provided, where each of the plurality of heating racks is a pre-assembled unit including a plurality of parallel pipes and a stand configured to secure the plurality of parallel pipes to the base of the biogas digester tank. The plurality of heating racks can be secured to the base, adjacent to the vertical wall. Each of the plurality of heating racks can be connected to a heating manifold arranged outside of the digester tank in parallel such that a heat exchange fluid is configured to independently flow from the heating manifold through the plurality of parallel pipes of each individual heating rack of the plurality of heating racks.

A method of carrying out a bioreaction in a multivessel bioreactor system may include flowing a culture medium at an initial flow rate through one or more fluidic paths between a master vessel and one or more slave vessels, detecting a first culture medium parameter value in the master vessel or the slave vessels, transmitting the first culture medium parameter value to a control system, determining an adjusted flow rate of the culture medium at the control system based on the first culture medium parameter value, and controlling a bidirectional fluid transfer device with the control system to adjust the flow rate of the culture medium through the one or more fluidic paths. The control system may adjust the flow rate of the culture medium to maintain a substantially uniform value of the first culture medium parameter value in the master vessel or the one or more slave vessels.

The invention relates to a method for a photochemical process, such as a photocatalytic and/or photosynthetic process, in particular for the culture and production or the hydroculture of microorganisms. A reaction medium (6) is conducted in a meandering manner in a reactor element (2) which is made of at least two upright and connected pipes (3) or chambers (13). Multiple reactor elements (2) are serially connected into a bio solar reactor (1), and a reaction medium (6) flow which is stress-free for the microorganisms is generated in the bio solar reactor (1) using hydrostatic pressure and level compensation. Inlet and outlet openings (4, 5) are arranged on the lower face (8) of each individual reactor element (2) on each of the outermost pipes (3) or chambers (13). The reaction medium (6) flows around all of the connections in the lower region, in particular the inlet opening (4), the outlet opening (5), and the introduction inlet (17). The invention also relates to a device for carrying out the method and to a bio solar reactor.

An enzymatic processing plant for continuous flow-based enzymatic processing of organic molecules. The enzymatic processing plant including an enzymatic processing area, wherein the enzymatic processing area includes a turbulence-generating pipe with a repeatedly changing centre-line and/or a repeatedly changing cross-section, for generating turbulence to mix a reaction mixture and prevent sedimentation of particles as the reaction mixture is flowing through the turbulence-generating pipe. The enzymatic processing plant and the enzymatic processing area are arranged such that the reaction mixture is subjected to turbulence within the enzymatic processing area for a reaction time of 15 minutes or more.

The invention discloses a condenser for a bioreactor exhaust, comprising: an inlet (1) adapted to be fluidically connected to a bioreactor exhaust port (2), a cooling chamber (3; 103) fluidically connected to the inlet and via a filter device (4) to an outlet (5), a cooling conduit (6; 106) in contact with the cooling chamber, a heating conduit (7) in contact with the filter device and a vortex tube (8) arranged to convey a cold gas stream through the cooling conduit and to convey a hot gas stream through the heating conduit.

The present invention provides a stem cell manufacturing system comprising: a sending channel (20) through which a solution containing cells flows; an apparatus (30) which is connected to the sending channel (20) and transfers a pluripotency inducer into the cells to produce cells harboring the inducer; and an apparatus (40) which cultures the cells harboring the inducer to produce cell clusters consisting of stem cells.