Disclosed cyclonic flow-inducing pumps overcome drawbacks associated with known adverse flow conditions that arise from flow of certain types of materials through a material flow conduit. Such cyclonic flow-inducing pumps provide for flow of flowable material within a flow passage of a material flow conduit (e.g., a portion of a pipeline, tubing or the like) to have a cyclonic flow (i.e., vortex or swirling) profile. Advantageously, the cyclonic flow profile centralizes flow toward the central portion of the flow passage, thereby reducing magnitude of laminar flow. Such cyclonic flow profile provides a variety of other advantages as compared to a parabolic flow profile such as, for example, increased flow rate, reduce inner pipeline wear, more uniform inner pipe wear, reduction in energy consumption, reduced or eliminated adverse considerations such as slugging.

Material flow amplifiers overcome drawbacks associated with known adverse flow conditions (e.g., surface erosion and head losses) that arise from flow of certain types of materials (e.g., fluids, slurries, particulates, flowable aggregate, and the like) through a material flow conduit. Such material flow amplifiers provide for flow of flowable material within a flow passage of a material flow conduit (e.g., a portion of a pipeline, tubing or the like) to have a cyclonic flow (i.e., vortex or swirling) profile. Advantageously, the cyclonic flow profile centralizes flow toward the central portion of the flow passage, thereby reducing magnitude of laminar flow. Such cyclonic flow profile provides a variety of other advantages as compared to a parabolic flow profile (e.g., increased flow rate, reduce inner pipeline wear, more uniform inner pipe wear, reduction in energy consumption, reduced or eliminated slugging and the like).

A device for emitting bubbles in a vehicle wash facility includes a plenum supported with respect to ground. The plenum includes an air inlet with a first area and an air outlet with a second area. The plenum air outlet is in communication with at least one foaming chamber. The foaming chamber includes a generally planar media element disposed therein. The foaming chamber includes a spray jet located therein, which is in communication with a source of chemical. The spray jet configured to emit a chemical onto the generally planar media element. The device also includes a plurality of nozzle portions in communication with the foaming chamber for emitting bubbles therefrom.

A device for emitting bubbles in a vehicle wash facility includes a plenum supported with respect to the ground. The plenum includes an air inlet with a first area and an air outlet with a second area. The plenum air outlet is in communication with at least one foaming chamber. The foaming chamber includes a generally planar media element disposed therein. The foaming chamber includes a spray jet located therein, which is in communication with a source of chemical. The spray jet configured to emit a chemical onto the generally planar media element. The device also includes a plurality of nozzle portions in communication with the foaming chamber for emitting bubbles therefrom.

An exhaust aftertreatment device for aftertreatment of exhaust gas of an internal combustion engine includes an SCR catalyst for selective catalytic reduction, a feeding apparatus for adding a reductant at an entry point upstream of the SCR catalyst to the exhaust gas, and a mixing apparatus arranged in a flow direction of the exhaust gas between the entry point and the SCR catalyst. The mixing apparatus includes a mixing element and a catalyst element, with the catalyst element having in the flow direction of the exhaust gas a cross sectional area which is smaller than a cross sectional area of the mixing element.

Some embodiments relate to a device for performing continuous emulsion of two immiscible fluids. The device includes: a first microsystem including at least two micro-channels for intake of each fluid, of different respective cross sections S1 and S2, which are offset and face each other along a central intake axis A; at least two micro-channels for output of the emulsion from the device once the emulsion is formed; and an area where the intake and output micro-channels intersect, the area being capable of generating an interface between the fluids and forming a pre-emulsion flowing in the output micro-channels until the emulsion is complete. The device also includes at least one singularity capable of destabilizing the interfaces between the fluids in the pre-emulsion.

Material flow amplifiers overcome drawbacks associated with known adverse flow conditions (e.g., surface erosion and head losses) that arise from flow of certain types of materials (e.g., fluids, slurries, particulates, flowable aggregate, and the like) through a material flow conduit. Such material flow amplifiers provide for flow of flowable material within a flow passage of a material flow conduit (e.g., a portion of a pipeline, tubing or the like) to have a cyclonic flow (i.e., vortex or swirling) profile. Advantageously, the cyclonic flow profile centralizes flow toward the central portion of the flow passage, thereby reducing magnitude of laminar flow. Such cyclonic flow profile provides a variety of other advantages as compared to a parabolic flow profile (e.g., increased flow rate, reduce inner pipeline wear, more uniform inner pipe wear, reduction in energy consumption, reduced or eliminated slugging and the like).

Disclosed cyclonic flow-inducing pumps overcome drawbacks associated with known adverse flow conditions that arise from flow of certain types of materials through a material flow conduit. Such cyclonic flow-inducing pumps provide for flow of flowable material within a flow passage of a material flow conduit (e.g., a portion of a pipeline, tubing or the like) to have a cyclonic flow (i.e., vortex or swirling) profile. Advantageously, the cyclonic flow profile centralizes flow toward the central portion of the flow passage, thereby reducing magnitude of laminar flow. Such cyclonic flow profile provides a variety of other advantages as compared to a parabolic flow profile such as, for example, increased flow rate, reduce inner pipeline wear, more uniform inner pipe wear, reduction in energy consumption, reduced or eliminated adverse considerations such as slugging.

A method for controlling fluid ratio accuracy during a dual flow injection with a powered injection system is described. The method includes predicting a first capacitance volume of a first syringe comprising a first medical fluid and a second capacitance volume of a second syringe comprising a second medical fluid with a first capacitance correction factor and a second capacitance correction factor, respectively, selecting a ratio of the first medical fluid and the second medical fluid to be administered to a patient in the dual flow injection, determining a relative acceleration ratio of a first piston of the first syringe and a second piston of a second syringe based on the predicted first capacitance volume and the predicted second capacitance volume, wherein the relative acceleration ratio is selected to maintain the selected ratio of the first medical fluid and the second medical fluid during the dual flow injection, and injecting a mixture of a first medical fluid and a second medical fluid having the selected ratio with the powered injection system.

A configuration for water purification undergoes the water supply step of taking in treatment water through a water suction port and pressure-feeding the treatment water, the air supply step of taking in air through an air suction port and supplying the air, the oxygen amount increasing step of pressurizing the air supplied at the air supply step to increase the total amount of oxygen, the ionization step of ionizing the pressurized air subjected to the oxygen amount increasing step, the mixing step of obtaining gas-liquid mixing fluid subjected to first fine air bubble formation by spraying the air into the flow of treatment water, and the accelerated spraying step of performing second fine air bubble formation by accelerating a flow velocity by a narrowed-diameter portion provided at a spray nozzle when the gas-liquid mixing fluid obtained through the mixing step is sprayed into the treatment water.