Abstract: Disclosed are a system and a method for dissolving water-soluble gas such as oxygen into water, employing microporous membrane.

Abstract: Disclosed are a system and a method for dissolving water-soluble gas such as oxygen into water, employing microporous membrane.

Abstract: A method and apparatus for micro-aeration of large scale fermentation systems is provided. The micro-aeration system includes a fermentation reactor, a sparging apparatus, and a micro-aeration gas mixture delivered to the fermentation reactor via the sparging apparatus. The micro-aeration gas mixture is a very low oxygen concentration mixture comprising: (i) an oxygen containing gas; and (ii) an inert carrier gas or reactive carrier gas that is recycled through the fermentation reactor. The gas mixture is introduced to the fermentation reactor at a minimum superficial velocity of about 0.04 m/sec to produce a uniform dispersion of the oxygen throughout the fermentation broth while concurrently mixing the entire fermentation broth. For a reactive gas consuming fermentation process, the amount of reactive carrier gas included as part of the gas mixture exceeds the reaction stoichiometric requirements in order to provide sufficient dispersion and agitation of the broth.

Abstract: A method and system for controlled rate freezing and nucleation of materials is provided. The presently disclosed system and method provides the ability to rapidly cool the materials contained in vials or other containers within a cooling unit via forced convective cooling using a laminar and uniform flow of cryogen in proximity to the plurality of vials disposed within the cooling unit. The rapid cooling of the biological materials is achieved by precisely controlling and adjusting the temperature of the cryogen being introduced to the system as a function of time. The presently disclosed methods to systems also provide nucleation control via temperature quench and depressurized nucleation control.

Abstract: A method and system for controlled rate freezing and nucleation of materials is provided. The presently disclosed system and method provides the ability to rapidly cool the materials contained in vials or other containers within a cooling unit via forced convective cooling using a laminar and uniform flow of cryogen in proximity to the plurality of vials disposed within the cooling unit. The rapid cooling of the biological materials is achieved by precisely controlling and adjusting the temperature of the cryogen being introduced to the system as a function of time. The presently disclosed methods to systems also provide nucleation control via temperature quench and depressurized nucleation control.

Abstract: A system and method for improved cryogenic cooling of process streams in polysilicon manufacturing is provided. The disclosed system and method provides for the cryogenic cooling of a silane and hydrogen process stream during the manufacture of polysilicon with concurrent recovery of refrigeration capacity from the vaporized nitrogen as well as the recovery of refrigeration capacity from the cold hydrogen stream. The improved cryogenic cooling system and method reduces the overall consumption of liquid nitrogen without sacrificing cooling performance of the cryogenic cooling of the silane and hydrogen process stream.

Abstract: A system and method for improved cryogenic cooling of process gases is provided. The disclosed system and method provides for the cryogenic cooling of a silane and hydrogen gas process stream during the manufacture of polysilicon with concurrent recovery of refrigeration capacity from the vaporized nitrogen as well as the recovery of refrigeration capacity from the cold hydrogen gas stream. The improved cryogenic cooling system and method reduces the overall consumption of liquid nitrogen without sacrificing cooling performance of the cryogenic cooling of the silane and hydrogen gas process stream.

Abstract: A method and apparatus for micro-aeration of large scale fermentation systems is provided. The micro-aeration system includes a fermentation reactor, a sparging apparatus, and a micro-aeration gas mixture delivered to the fermentation reactor via the sparging apparatus. The micro-aeration gas mixture is a very low oxygen concentration mixture comprising an oxygen containing gas and an inert carrier gas that is preferably recycled through the fermentation reactor. The inert carrier gas is preferably nitrogen whereas the oxygen containing gas is oxygen or and is introduced to the fermentation reactor at a minimum superficial velocity of about 0.02 m/sec to produce a uniform dispersion of the oxygen/air throughout the fermentation broth while concurrently mixing the entire fermentation broth. The micro-aeration method and apparatus further comprises a controller operatively coupled to one or more control valves for regulating the micro-aeration conditions in the fermentation reactor.

Abstract: A method and system for controlled rate freezing and nucleation of biological materials is provided. The presently disclosed system and method provides the ability to rapidly cool the materials contained in vials or other containers within a cooling unit via forced convective cooling and optionally simultaneous pressure drop using uniform and unidirectional flow of cryogen in proximity to the plurality of vials disposed within a cooling unit. The rapid cooling of the biological materials is achieved by precisely controlling and adjusting the temperature of the cryogen being introduced to the system as well as the chamber pressure as a function of time.

Abstract: A method and apparatus for condensing vapor in a gas. A cryogen, such as liquid nitrogen, may be provided into first and second coil sets in a condenser housing to cool the condensable vapor in the housing to condense the vapor into a liquid or solid form. The flow of cryogen in the first and second coil sets may be independently controlled, coils in the first and/or second coil sets may have a substantially equal length, and/or coils in the first and/or second coil sets may have uppermost portions that are located at a substantially equal height.

Abstract: Oxygen is delivered into a liquid contained within a vessel. Oxygen-rich gas is introduced at an inner mixing region of a vessel toward an agitating element for dissolving some of the oxygen into the liquid. Air is introduced to the liquid at a location different from where the oxygen-rich gas is introduced, minimizing coalescing of bubbles of the oxygen-rich gas and air bubbles. Running the agitating element in the vessel may induce mixing of the liquid and improve oxygen dissolution. Movement of the air bubbles can also generate a mixing effect on the liquid, yet independent from mixing caused by the agitating element. In some embodiments, currents produced by the agitating element are asymmetric with respect to a vertical axis of the vessel. Air bubbles may also form an asymmetric configuration of bubbles about the vertical axis.

Abstract: A disposable mixing vessel incorporates a system for dynamic gas control. The disposable mixing vessel includes a first agitating element and a second agitating element located above the first agitating element. The system for dynamic gas control enables a cell culture process to occur in the disposable mixing vessel while maintaining certain parameters of the liquid medium to be within a desired range. Such parameters may include the level of dissolved carbon dioxide, the level of dissolved oxygen, the pH and the osmolality. The system for dynamic gas control may control gas inlet and outlet ports in the disposable mixing vessel for sweeping a suitable composition of gas across the headspace of the liquid medium.

Abstract: Biological liquid substances in a disposable bioreactor or a disposable fermentor is enriched with a dissolved gas such as oxygen. The gas is provided to the liquid in meeting growth needs of biomass within the disposable vessel. The liquid is processed through a bubble forming element such as a supersonic mixer, a membrane sparger, or the like, to form a gas-liquid dispersion. The dispersion has a high interfacial surface area for facilitating gas dissolution in the liquid. Receptacles of the disposable vessel may be coupled (e.g., magnetically) to one or more processing devices (e.g., motors, pumps, gas sources) outside of the disposable vessel so that components within the disposable vessel are able to perform functions suitable for furthering reaction and/or fermentation processes.

Abstract: A method and system for controlled rate freezing and nucleation of materials is provided. The presently disclosed system and method provides the ability to rapidly cool the materials contained in vials or other containers within a cooling unit via forced convective cooling using a laminar and uniform flow of cryogen in proximity to the plurality of vials disposed within the cooling unit. The rapid cooling of the biological materials is achieved by precisely controlling and adjusting the temperature of the cryogen being introduced to the system as a function of time. The presently disclosed methods to systems also provide nucleation control via temperature quench and depressurized nucleation control.

Abstract: A method and system for controlled rate freezing and nucleation of materials is provided. The presently disclosed system and method provides the ability to rapidly cool the materials contained in vials or other containers within a cooling unit via forced convective cooling using a laminar and uniform flow of cryogen in proximity to the plurality of vials disposed within the cooling unit. The rapid cooling of the biological materials is achieved by precisely controlling and adjusting the temperature of the cryogen being introduced to the system as a function of time. The presently disclosed methods to systems also provide nucleation control via temperature quench and depressurized nucleation control.

Abstract: The tendency of carbonated beverage to generate excessive foam when it is produced and bottled is reduced in a process including: (a) providing water or a mixture of water and syrup, which contains oxygen or air dissolved therein, and maintaining a pressure greater than atmospheric thereon; (b) saturating said mixture with carbon dioxide, and feeding the resultant mixture to step (c), while maintaining sufficient pressure thereon that no dissolved gas evolves therefrom; and (c) removing dissolved oxygen or air from the mixture formed in step (b) while dissolving additional carbon dioxide into said mixture and maintaining over said mixture a pressure greater than atmospheric.

Abstract: A direct contact cryogenic crystallizer having a vertically oriented draft tube into which cryogenic fluid is injected at a high velocity along with warm gas and through which a crystal slurry is drawn for subsequent cooling and agitation for the production of crystals.

Abstract: A direct contact cryogenic crystallizer having a vertically oriented draft tube into which cryogenic fluid is injected at a high velocity along with warm gas and through which a crystal slurry is drawn for subsequent cooling and agitation for the production of crystals.

Abstract: The dispersion of a gas in a liquid is enhanced by accelerating a gas/liquid mixture to supersonic velocity, with subsequent deacceleration, in a conical in-line mixer.

Abstract: An in-line stripper has a venturi-conical mixer combination in which the annular space thereby is automatically adjustable in response to changes in viscosity or other property conditions.