Abstract: The metering device comprises a housing, defining at least one inlet for the material to be metered and at least one outlet for that material, and at least one rotatable ball driven by a shaft, the ball having a transverse bore containing a shuttling ball moving linearly in the bore between two seats and seals against the one or the other seat. The rotatable ball is captured between the seats and seals under pressure against the outlet seat. Such a metering device allows an exact metering, in shot or rapid shot resulting in near continuous flow form, has great simplicity of construction with few working parts such as that it may easily be placed at the dispensing end of a pressure transfer system for liquids and gases and acts as shut off valve between metering use such that it prevents stalled hydrostatic fluid pressure behind the metering device from causing a flow surge ahead of the metering device at start up.

Abstract: An apparatus for proportioning and dispensing at least two different fluid compositions having different degrees of compressibility includes a cartridge having therein plural separate chambers for containing separate fluid compositions to be proportioned and dispensed. A neck portion is provided at a discharging end of the cartridge. Plural separate passageways extend through the neck portion, each passageway opening into a separate respective chamber. Structure is provided for controlling the flow of the fluid compositions through the respective passageways, for preventing run-on of the fluid compositions through the respective passageways due to decompression of the fluid compositions upon removal of an extruding pressure, and thereby for preventing dispensing of the fluid compositions through the respective passageways in proportional ratios other than a desired predetermined proportional ratio. Such structure includes a valve member having therethrough plural passage portions.

Abstract: A mixer mixes at least two fluid components of the type which when mixed together undergo chemical reaction to form a solid or semi-solid reaction product. The components are separately introduced into the mixer, whereat they are mixed, and the reaction mixture is discharged from the mixer prior to the completion of the chemical reaction and while still in a fluid state. When desired, for example when it is necessary to shut down the operation of the mixer, the chemical reaction in the mixer is arrested by selectively cooling the reaction mixture down to a temperature at which the chemical reaction will not occur or will at least be retarded. This prevents the formation of the reaction product within the final mixer. Thereafter, for example when the operation of the mixer is again commenced, the reaction mixture is reheated to an increased temperature at which the chemical reaction will continue.

Abstract: A fluid stream including separate layers of plural components is mixed by dividing the fluid stream into a plurality of substreams, reorienting and recombining the substreams in a chamber, and repeating the steps of dividing, reorienting and recombining until a desired degree of mixing of the components is obtained. The substreams of a given stage or group of substreams are controlled so that the substreams are longitudinally dephased with respect to each other such that the fluids of the substreams are longitudinally blended when recombined. The dephasing is achieved by providing that at least selected of the passageways for the substreams of a given stage of the mixer are dimensioned such that the total resistances to flow of the fluid of the substreams passing through the selected passageways, from the beginnings thereof to the ends thereof, are unequal.