The present disclosure provides advantageous rotary interfaces for fluid assemblies (e.g., rotary interfaces for fluid flow in bioreactor applications), and related methods of fabrication and use. More particularly, the present disclosure provides improved rotary interfaces for fluid flow through porous impellers for filtration and/or sparging for fluid assemblies (e.g., bioreactor applications), and related methods of fabrication and use. Disclosed herein is a fluid assembly (e.g., bioreactor) that includes a porous impeller which is in fluid communication with a hollow shaft that can be used to transport a reaction fluid to an external storage tank or the like. The fluid assembly/bioreactor can include a coupling mechanism that transmits rotary motion from a motor to a primary shaft and then to a hollow secondary shaft, while at the same time permitting removal of a filtrate from the fluid assembly or bioreactor via the hollow secondary shaft and a porous impeller.

A filter apparatus is disclosed for withdrawing a fluid medium from a bioreactor during the growth of a cell culture within the bioreactor. Also disclosed is a method for culturing cells in a bioreactor. The filter apparatus includes a hollow tubular member attached to a filter member. The filter member has a pore size and volume capable of withdrawing a fluid medium at a relatively high flow rate from the bioreactor. Without withdrawing biological cells from the bioreactor and without damaging or harming the cells. The filter apparatus of the present disclosure allows for many process improvements.

A cell purification module, configured to purify multiple cells from a fluid sample is provided. The cell purification module includes a hollow column, multiple hollow fiber membranes, at least one first magnetic component, a fluid sample inlet end, and a fluid sample outlet end. The hollow column has a first opening, a second opening, and an accommodating space connecting the first opening and the second opening. The hollow fiber membranes are disposed in the accommodating space and each hollow fiber membrane has multiple pores. The first magnetic component is disposed at a periphery of the hollow column. The fluid sample inlet end and the fluid sample outlet end are respectively disposed at two ends of the hollow column. The hollow fiber membranes extend in an axial direction of the hollow column, and are arranged in a radial direction of the hollow column. A cell purification system is also provided.

An object of the present invention is to provide a separation substrate having a high megakaryocyte blocking rate and a high platelet permeation rate, and a cell separation filter and a method for producing a platelet which use the same. The separation substrate of the present invention is a separation substrate including non-woven fabric for separating a platelet from a cell suspension containing a megakaryocyte and the platelet, in which an average pore diameter of the separation substrate is 2.0 μm to 15.0 μm, and a thickness of the separation substrate is 10 μm to 500 μm.

A bioreactor for producing hydrogen gas and other metabolites. The bioreactor utilizes light, fermentation, and other metabolic processes for the production of metabolites, derived from various microorganisms contained within the bioreactor through respective metabolic pathways. The bioreactor comprises a main reactor chamber, a semipermeable membrane, a sleeve, a power supply, a substrate medium, a heating member, a plurality of tubing members, a collection reservoir, a pressure-sealed connecter member, and an agitator.

This invention relates to compositions of matter, methods, modules and automated, end-to-end closed instruments for automated mammalian cell growth, reagent bundle creation and mammalian cell transfection followed by nucleic acid-guided nuclease editing in live mammalian cells. The disclosed compositions and method entail making “reagent bundles” comprising many (hundreds of thousands to millions) clonal copies of an editing cassette and delivering or co-localizing the reagent bundles with live mammalian cells such that the editing cassettes edit the cells and the edited cells continue to grow.

Provided are a method and a system for culturing cells and harvesting biologics. More particularly process for cell culture by intensified perfusion with continuous harvest and without cell bleeding is provided.

A system for buoyant particle processing includes: a reaction vessel, a stirring mechanism, a set of one or more pumps, and a filter. The system can additionally or alternatively include a set of pathways and/or any other suitable component(s). A method for buoyant particle processing includes: stirring the contents of a reaction vessel; washing a set of buoyant particles; and filtering the contents of the reaction vessel. Additionally or alternatively, the method can include any or all of: preprocessing the set of buoyant particles; adding a set of inputs to the reaction vessel; washing the set of buoyant particles; repeating one or more; and/or any other suitable process(es).

The membrane bioreactor for simultaneous enzymatic cellulose hydrolysis and product separation is a vessel having a lower hydrolysis reaction chamber and an upper distilled water chamber separated by a semipermeable membrane attached to the top of the lower reaction chamber. The membrane is supported on a stainless steel mesh and sealed to the mesh by epoxy glue to prevent leakage. A peristaltic pump is connected to the reaction chamber and maintains a flow of distilled water through the membrane and the upper chamber, the effluent being collected in a beaker or other product collection vessel. The reaction chamber is agitated at a moderate rate by a magnetic stirrer, and the upper chamber is agitated more rigorously by a mechanical stirrer. A thermocouple and temperature controller and a buffer solution, respectively, maintain temperature and pH in the reaction chamber optimal for enzymatic hydrolysis of cellulose.

A cell processing system comprising an enclosure 601, an outer enclosure 701 that envelops the enclosure 601, an intake air purification filter 602 provided in the enclosure 601, that purifies gas that has been drawn in from outside the enclosure 601, a circulating apparatus, inside the outer enclosure 701, that circulates gas inside and outside the enclosure 601 in such a manner that gas in the outer enclosure 701 is drawn into the enclosure 601 through the intake air purification filter 602 and gas inside the enclosure 601 is discharged into the outer enclosure 701, and a cell processing apparatus for processing of cells, disposed inside the enclosure 601.