Abstract: Control of humidity in chemical reactors, and associated systems and methods, are generally described. In certain embodiments, the humidity within gas transport conduits and chambers can be controlled to inhibit unwanted condensation within gas transport pathways. By inhibiting condensation within gas transport pathways, clogging of such pathways can be limited (or eliminated) such that transport of gas can be more easily and controllably achieved. In addition, strategies for purging condensed liquid from chemical reactor systems are also described.

Abstract: Control of humidity in chemical reactors, and associated systems and methods, are generally described. In certain embodiments, the humidity within gas transport conduits and chambers can be controlled to inhibit unwanted condensation within gas transport pathways. By inhibiting condensation within gas transport pathways, clogging of such pathways can be limited (or eliminated) such that transport of gas can be more easily and controllably achieved. In addition, strategies for purging condensed liquid from chemical reactor systems are also described.

Abstract: Control of humidity in chemical reactors, and associated systems and methods, are generally described. In certain embodiments, the humidity within gas transport conduits and chambers can be controlled to inhibit unwanted condensation within gas transport pathways. By inhibiting condensation within gas transport pathways, clogging of such pathways can be limited (or eliminated) such that transport of gas can be more easily and controllably achieved. In addition, strategies for purging condensed liquid from chemical reactor systems are also described.

Abstract: Methods of calibrating a pH sensor fixed within an enclosed vessel are disclosed. The methods include introducing a buffer into the enclosed vessel, introducing a gas mixture comprising CO2 into the enclosed vessel, measuring a pH signal of the solution, measuring a CO2 concentration of a headspace gas of the solution, and calculating a pH value with a buffer calibration curve. The methods include calculating a calibration parameter with a sensor calibration curve and calibrating the pH sensor with the calibration parameter. Reactor systems are also disclosed. The systems include an enclosed reactor, a pH sensor, a CO2 sensor, a temperature control subsystem, and a controller. Methods of facilitating pH sensor calibration without sampling in a bioreactor system are also disclosed. The methods include providing a controller and providing instructions to operably connect the controller to the pH sensor and the CO2 sensor.

Abstract: Control of humidity in chemical reactors, and associated systems and methods, are generally described. In certain embodiments, the humidity within gas transport conduits and chambers can be controlled to inhibit unwanted condensation within gas transport pathways. By inhibiting condensation within gas transport pathways, clogging of such pathways can be limited (or eliminated) such that transport of gas can be more easily and controllably achieved. In addition, strategies for purging condensed liquid from chemical reactor systems are also described.

Abstract: Control of humidity in chemical reactors, and associated systems and methods, are generally described. In certain embodiments, the humidity within gas transport conduits and chambers can be controlled to inhibit unwanted condensation within gas transport pathways. By inhibiting condensation within gas transport pathways, clogging of such pathways can be limited (or eliminated) such that transport of gas can be more easily and controllably achieved. In addition, strategies for purging condensed liquid from chemical reactor systems are also described.

Abstract: A microreactor with a reaction chamber comprising two sub-chambers with reconfigurable volumes, an input conduit with input valve, an un-filtered output conduit with first output valve, and a filtered output conduit with a second output valve is used to perform a method to control a different dilution rate for cells and molecules in continuous culture bioprocesses. In preferred embodiments flow control is achieved using the difference in volume of the two sub-chambers.

Abstract: The present invention provides apparatus and methods to operate microreactor devices through the controlled delivery of pressurized fluids. A heated reservoir, a heated manifold, and a heater for the microreactor device provides for the delivery of a pressurized gas while minimizing evaporation and condensation; and a fluid interface and pressure interlock provides for the delivery of aseptic fluids while minimizing contamination and fluid loss.

Abstract: The present invention provides apparatus and methods for measuring the optical density of a fluid by measuring the light transmission through a reconfigurable optical path. The optical path is reconfigured by the deflection of an elastic membrane wherein the optical path length through the fluid is determined by the position of the membrane relative to a fixed surface. The optical density can be determined from two measurements with different optical path lengths through the fluid.

Abstract: Devices, systems, and methods for continuous cell culture and other reactions are generally described. In some embodiments, chambers (e.g., cell growth chambers) including at least a portion of a wall formed of a flexible member are provided. A retaining structure can be incorporated outside and proximate to the chamber such that when liquid is added to the chamber, the flexible member is consistently and predictably deformed, and a consistent volume of liquid is added. The flexible member can be formed of, in some embodiments, a gas-permeable medium. In some embodiments, reaction chambers can be arranged in a fluidic loop, and a bypass channel can be used to introduce and/or extract fluid from the loop without affecting loop operation.

Abstract: A microreactor with a reaction chamber comprising two sub-chambers with reconfigurable volumes, an input conduit with input valve, an un-filtered output conduit with first output valve, and a filtered output conduit with a second output valve is used to perform a method to control a different dilution rate for cells and molecules in continuous culture bioprocesses. In preferred embodiments flow control is achieved using the difference in volume of the two sub-chambers.

Abstract: Control of humidity in chemical reactors, and associated systems and methods, are generally described. In certain embodiments, the humidity within gas transport conduits and chambers can be controlled to inhibit unwanted condensation within gas transport pathways. By inhibiting condensation within gas transport pathways, clogging of such pathways can be limited (or eliminated) such that transport of gas can be more easily and controllably achieved. In addition, strategies for purging condensed liquid from chemical reactor systems are also described.

Abstract: Devices, systems, and methods for continuous cell culture and other reactions are generally described. In some embodiments, chambers (e.g., cell growth chambers) including at least a portion of a wall formed of a flexible member are provided. A retaining structure can be incorporated outside and proximate to the chamber such that when liquid is added to the chamber, the flexible member is consistently and predictably deformed, and a consistent volume of liquid is added. The flexible member can be formed of, in some embodiments, a gas-permeable medium. In some embodiments, reaction chambers can be arranged in a fluidic loop, and a bypass channel can be used to introduce and/or extract fluid from the loop without affecting loop operation.

Abstract: Parallel, integrated bioreactor. The bioreactor includes a plurality of growth chambers, each growth chamber associated with a peristaltic oxygenating mixer and separated therefrom by a porous membrane. Each oxygenating mixture has a gas inlet and a gas outlet with the gas inlet in fluid communication with a gas reservoir. A gas mixer switch is provided for controlling oxygen concentration in the reservoir. The apparatus and methods disclosed in the application allow precise control over dissolved oxygen concentration with a quick response time.