An NO-accumulation apparatus, method and use, comprising: a container (120) defining a cavity for accommodating a liquid (105), an inlet (150) for feeding the liquid into the container (120) and an outlet (151) for delivering the liquid from the container (120) to a bath unit; an NO-gas dissolving unit (140) for dissolving gaseous NO in the liquid (105) to produce an NO-containing liquid, wherein the NO-gas dissolving unit (140) is arranged in the container (120) and/or forms a part of the container (120); and an NO-gas port (110) in fluid communication with the NO-gas dissolving unit (140), wherein the NO-gas port (110) is adapted for coupling, particularly for releasably coupling, with an NO-gas supply, whereby the apparatus further comprises means for decoupling the inflow of NO to the liquid (105) within the container from the removal of the NO-containing liquid (NO-decoupling means), so that the removal of the NO-containing liquid is inhibited, when the NO is flowing into the liquid, and also the NO inflow is inhibited when the NO-containing liquid is removed from the container (105).

The present disclosure relates to a device for producing microbubble water by using a ultrasonic vibrator having a maximized amount of dissolved bubbles, a microbubble discharge unit, cell culture medium containing microbubble water and cell culturing method using the same, a high-efficiency mixed fuel using microbubble and apparatus for manufacturing the same.

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

A system for gas impregnation of a liquid includes a container for holding a product ingredient, a first still liquid conduit for conveying a still product including the ingredient, a gas cylinder providing a gas conduit with a compressed gas such as Nitrogen. The system includes two or more pressure chambers each having a corresponding liquid fill valve to control the flow of a still product filling the pressure chamber, and a gas diffuser for diffusing the compressed gas into the still product to produce a gas infused product. A multi-way valve in fluid communication with each of the pressure chambers directs the gas infused product from a selected one of the pressure chambers to a first charged product conduit for supplying a charged liquid dispenser, and blocks fluid from flowing from other, non-selected, ones of the pressure chambers. A method for using the subject system is also provided.

A process and apparatus for separating components of a source gas is provided in which more soluble components of the source gas are dissolved in an aqueous solvent at high pressure. The system can utilize hydrostatic pressure to increase solubility of the components of the source gas. The apparatus includes gas recycle throughout multiple mass transfer stages to improve mass transfer of the targeted components from the liquid to gas phase. Separated components can be recovered for use in a value added application or can be processed for long-term storage, for instance in an underwater reservoir.

The systems and methods disclosed herein provide for the efficient generation of fine bubbles. In particular, systems and methods for use in bioreactors are disclosed herein providing a superior means to produce useful fermentation products by the biological fermentation of fine bubble waste substrates injected into a liquid broth containing a microorganism culture.

An apparatus for producing carbonated water includes a gas cylinder configured to store carbon dioxide gas, a cold water storage unit configured to store cold water, a producing tank defining a closed space where the carbonated water is produced, a water supply passage configured to connect the cold water storage unit to the producing tank, the water supply passage including a water supply valve that controls supply of the cold water, a gas supply passage connecting the gas cylinder to the producing tank, the gas supply passage including a gas valve that controls supply of the carbon dioxide, a first relief valve provided along the gas supply passage, the first relief valve configured to control the discharge of the carbon dioxide gas, a dispensing passage connecting the producing tank to a dispensing member, and the dispensing member configured to dispense the carbonated water from a front surface of a refrigerator.

A gas diffusion system configured to feed a gas stream, in particular a passivating gas stream, into an apparatus, in particular a decomposer, of a urea plant; the system extends along an axis and has a gas feed conduit having an outlet from which the gas flows substantially parallel to the axis, and a diffuser assembly configured to diffuse the gas supply from the conduit; the diffuser assembly is shaped so as to intercept the gas stream flowing axially from the outlet, and divert the gas stream substantially radially with respect to the axis and uniformly about the axis.

A water aeration diffuser has a base with an internal cavity defining an air pocket, and a ceramic plate removably attached to the base. The base is in flow communication with air supply such that air is received in the cavity and then diffused by the ceramic plate to create an aeration column in a body of water. To allow for repair and servicing, the ceramic plate is removably attached to the base by one or more fasteners. The base includes a perimeter lip around its top portion that supports the ceramic plate and maximizes the exposed surface area of the plate. A water and air-tight gasket is provided between the lip and the ceramic plate. An eye-bolt may be provided through the ceramic plate and attached to the base to provide an attachment point for a ballast or other means used to position the diffuser.

A method and apparatus for injecting a gas into a liquid in which a rotating helical impeller within a draft tube submerged in the liquid creates a liquid flow within the draft tube. Gas bubbles are injected into the draft tube either above or below or alongside the helical impeller or in all three locations. The liquid is drawn into the draft tube with a superficial velocity greater than a substantially uniform terminal ascent velocity of the gas bubbles to allow entrainment of undissolved gas bubbles in the bulk liquid into the liquid being drawn into the draft tube. The gas bubbles are injected with a uniform diameter of between about 10.0 microns and about 1.0 millimeters. The small bubble size enhances the dissolution of the gas into the liquid and also allow the entrainment of the gas into the liquid being drawn into the draft tube.