Flow Mixers TRIZ Cases

Z-type channels segment flow to reduce average oil droplet size, preventing aggregation and coalescence that compromise emulsion stability.

Dual rotors in a reaction pump split hydrocarbons through viscous heating, lowering process temperatures to prevent side reactions that reduce fuel yield.

External circulation between a pulping machine and kneading tank resolves inadequate mixing in one-pass processes by enabling repeated dispersion.

Angled guide blades in a flat cross-section carrier redirect exhaust flow to prevent wall film formation and ensure complete reducing agent evaporation.

Dispersion of wet polymer filtration cake in dimethyl sulfoxide eliminates hazardous drying steps, reducing energy consumption and equipment complexity.

Segmented gas flow drives rapid aeration while expansion chamber prevents bubble overflow during high-volume injection.

Laser welding joins spiral blades to tube walls, enabling fine intervals that increase surface area and mixing efficiency.

Axial movement of the dosing mandrel clears accumulated particles from the agent passage, resolving dosage accuracy versus clogging resistance.

Pressurized pumps deliver components to a rotating body for mixing, eliminating residual volume in static mixers.

Recirculation loops in a central mixing tank maintain steady flow rates, reducing lot-to-lot variations below 1% while increasing throughput.

Segmented blades with specific angles of incidence generate swirling motion that accelerates liquid evaporation and prevents droplet breakthrough.

Cyclic shear forces from a rotating vane assembly control droplet size uniformity, resolving continuous shear trade-offs.

A trickling mixture forms a labyrinth seal in connecting channels to maintain pressure differentials without airlocks.

Sector openings and swirler vanes create rotational flow patterns that improve NOx sensor accuracy by ensuring uniform gas composition.

A pump-mixer combines fluid transportation and vigorous mixing to disperse treating agents uniformly within a single processing tank.

Flow-dividing layers deflect marginal flows to prevent phase separation and demixing in continuously expanding diffusers.

A gas discharge member with sub-micron pores generates nano-order bubbles when liquid flows at high velocity across the surface.

A water carbonation unit uses a merging duct to combine pressurized carbon dioxide and water streams before entering a mixing chamber.

Mounting a doser tangentially on an exhaust mixer directs urea spray against swirling gas flow to reduce deposit formation.

Swirl plates and fan blades rotate exhaust gas to atomize urea, preventing crystal formation on the mixing tube wall during low load operation.

A dispenser adjusts liquid turbulence to dissolve solid products into a solution.

Integral vanes and variable cross-section doser chambers ensure uniform diesel exhaust fluid distribution, resolving complexity trade-offs in SCR systems.

Turbulent microfluidic mixing accelerates antibody-antigen binding kinetics, eliminating incubation delays and enabling real-time analyte detection.

Compressing bulk and additive streams increases interfacial area, preventing polymer build-up and pressure loss in laminar flow.

A compact exhaust mixer uses a flow diverter orifice to accelerate gas along the inner wall for thorough fluid spray mixing.

A circulating dispersing system uses an adjusting valve to control mixture flow between two tanks for uniform processing.

An inclined mixer member with fins collides with obliquely injected urea water, resolving uneven reducing agent distribution that causes excessive ammonia slip.

Secondary channel actuators create transverse flows that reduce dead volumes and improve mixing completeness in laminar regimes.

A spiral housing section creates rotationally symmetrical flow conditions that prevent asymmetrical spray patterns and particle filter clogging.

A centrifugal blender assembly mixes particulates with liquids using a dedicated expeller and separate pumps.

Linear monopole magnetic fields break molecular bonds in regulated flow streams while turbulence-inducing obstructions create chaotic mixing for new compositions.

Liquid carbon dioxide injection eliminates gas headspace waste and oxygen contamination while enabling precise dissolved gas ratio control.

A liquid mixture nozzle accelerates fluid through a converging section and orifice to generate shear forces.

A venturi with a movable pod adjusts geometry to improve media mixing efficiency across varying pressure conditions.

A bottom-up liquid filling system uses a spring-driven lifting member to push fluid upward through a retractable tube assembly.

A dense phase powder supply system uses a straight gas blowing tube to inject gas locally into a gravity-fed truncated cone for stable flow.

A perpendicular tube mixer redirects exhaust flow to enhance gas homogeneity.

A proportioner uses a dynamic restrictor assembly to control foam concentrate flow through an annulus formed by a movable disk and orifice plate.

Injection quills deliver immiscible co-catalyst streams into ionic liquid catalysts using elevated flow velocity for uniform mixing.

A liquid dispenser dosing chamber uses a vent system to break air locks and enable treating liquid flow.

Multi-stage mixer generates swirl flow to distribute reductant, reducing pressure drop and deposit formation in aftertreatment systems.

A compact exhaust treatment device integrates reactant dosing and a swirl chamber to generate turbulence for uniform mixing.

High-pressure nozzles shear drilling fluid to reduce noise and wear while maintaining composition stability.

Inclined coplanar segments deflect fluid flow to generate large-scale vortices, ensuring rapid additive homogenization under short mixing length constraints.

A fluidic premixer uses a movable shutter to regulate Venturi suction and maintain precise additive metering across varying flow rates.

Blades with small angles of attack reduce pressure loss while maintaining mixture homogeneity.

Passive elements in the discharge cap disrupt fluid velocity to prevent air entrapment and oxidation at low levels.

Homogenizing blends above 400 kg/cm2 accelerates reaction rates while minimizing glycerol byproducts.

A vortex-type mixing device enhances gas and liquid phase homogeneity in down-flow reactors using inwardly-directed vanes.