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Hydrodynamic Cavitation Technological Equipment
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Nomenclature
Unless otherwise stated, quantities are expressed in SI units. Subscripts identify the relevant station, phase, component, or energy boundary.
| Symbol | Definition | SI unit or status |
|---|---|---|
| A | Flow cross sectional area | m² |
| Ao | Total orifice open area | m² |
| Ap | Pipe cross sectional area | m² |
| At | Venturi throat area | m² |
| C0 | Initial concentration | Application dependent |
| Cn, Ct | Concentration after n passes or treatment time t | Application dependent |
| Cd | Discharge coefficient | Dimensionless |
| cp | Specific heat capacity | J kg⁻¹ K⁻¹ |
| D | Pipe, rotor, or characteristic diameter | m |
| Dh | Hydraulic diameter | m |
| D10, D50, D90 | 10th percentile, median, and 90th percentile of a size distribution | m or μm |
| d32 | Sauter mean droplet diameter | m or μm |
| do | Orifice diameter | m |
| dt | Throat diameter | m |
| Eel | Electrical input energy | J or kWh |
| Eh | Hydraulic energy across cavitation device | J |
| Ein | Selected input energy for yield calculation | J or kWh |
| Eu | Euler number | Dimensionless |
| f | Frequency | s⁻¹ |
| fs | Vortex shedding frequency | s⁻¹ |
| g | Gravitational acceleration | m s⁻² |
| Irreversible head loss | m | |
| kpass | Apparent first order per pass coefficient | pass⁻¹ |
| L | Length or characteristic length | m |
| mb | Processed batch mass | kg |
| ṁ | Mass flow rate | kg s⁻¹ |
| n | Rotational frequency or number of passes, as defined | s⁻¹ or dimensionless |
| Nh | Number of holes | Dimensionless |
| Np | Nominal number of passes | Dimensionless |
| p | Static pressure | Pa |
| Pressure inside a cavity | Pa | |
| pref | Reference pressure used in cavitation number | Pa |
| pv | Vapor pressure at liquid temperature | Pa |
| Pact | Active or reference volume for power density | m³ |
| Pel | Measured electrical input power | W |
| Ph | Hydraulic power across cavitation device | W |
| Pshaft | Pump or rotor shaft power | W |
| Q | Volumetric flow rate | m³ s⁻¹ |
| R | Cavity radius or rotor radius, as defined | m |
| Re | Reynolds number | Dimensionless |
| ReΩ | Rotational Reynolds number | Dimensionless |
| SEC | Specific energy consumption | J kg⁻¹ or kWh t⁻¹ |
| St | Strouhal number | Dimensionless |
| t, tp | Time and processing time | s |
| U, v | Characteristic or mean velocity | m s⁻¹ |
| utip | Rotor tip speed | m s⁻¹ |
| V | Volume | m³ |
| Vactive | Defined active device volume | m³ |
| Vb | Total recirculating batch and loop volume | m³ |
| We | Weber number | Dimensionless |
| YC | Concentration change yield per input energy | Application dependent |
| z | Elevation | m |
| a, b, c, d | Empirical coefficients in the vortex device Euler number correlation | Dimensionless |
| CP | Rotating device power coefficient | Dimensionless |
| Erecovered | Recovered useful thermal or mechanical energy credited to the process | J or kWh |
| Eu* | Scaled Euler number, Eu/50 in the cited vortex correlation | Dimensionless |
| fp | Nominal rotor element passage frequency | s⁻¹ |
| Ne | Number of cavitation generating elements encountered per revolution | Dimensionless |
| Nexp | Nominal number of cyclic exposures in the active region | Dimensionless |
| Nparallel | Number of parallel cavitation units or trains | Dimensionless |
| Jet dynamic pressure | Pa | |
| Ploss | Mechanical, electrical, and environmental power loss within the declared boundary | W |
| Q̇rem | Rate of heat removed by a cooler or heat exchanger | W |
| Q̇ret | Rate of heat retained in the processed stream | W |
| Re* | Scaled Reynolds number, Re/1000 in the cited vortex correlation | Dimensionless |
| SECnet | Net specific electrical energy after an explicitly stated recovered energy credit | J kg⁻¹ or kWh t⁻¹ |
| T | Measured shaft torque | N m |
| tres | Mean residence time in the active cavitation region | s |
| urel | Relative velocity across a rotor stator clearance | m s⁻¹ |
| VT | Vortex device throat velocity | m s⁻¹ |
| Vθ, max | Maximum tangential velocity in a vortex chamber | m s⁻¹ |
| An | Total nozzle area in a high pressure interaction cell | m² |
| APM | Auxiliary Processing Module | abbreviation |
| Bp | Backpressure ratio | dimensionless |
| Cv | Jet velocity coefficient | dimensionless |
| CIP | Clean in place | abbreviation |
| EC | Pion BEE Emulsifying Cell | abbreviation |
| eh | Hydraulic energy per unit mass | J kg−1 |
| GMP | Good manufacturing practice | abbreviation |
| HPH | High pressure homogenization | abbreviation |
| IXC | Microfluidics Interaction Chamber | abbreviation |
| Lc | Distance from nozzle to principal recovery or impact region | m |
| pb | Controlled downstream backpressure | Pa |
| Pj | Jet kinetic power scale | W |
| tc | Mean cavity transport time to recovery region | s |
| vj | Characteristic jet velocity | m s−1 |
Greek Letters
| Symbol | Letter name | Meaning |
|---|---|---|
| α | Alpha | Phase volume fraction or geometric angle when explicitly defined |
| β | Beta | Diameter ratio do/D or throat ratio |
| γ | Gamma | Surface or interfacial tension |
| Δ | Delta | Difference or change, such as pressure drop Δp |
| ε | Epsilon | Turbulent or cavitation induced energy dissipation rate |
| η | Eta | Efficiency; subscripts identify hydraulic, motor, drive, or process efficiency |
| λ | Lambda | Scale ratio for length, flow, or pressure |
| μ | Mu | Dynamic viscosity |
| ν | Nu | Kinematic viscosity when used |
| ρ | Rho | Density |
| σ | Sigma | Cavitation number |
| φA | Phi | Total open area fraction |
| ω | Omega | Angular velocity |
| π | Pi | Circular constant |
| δ | Delta, lowercase | Rotor stator gap or mechanical clearance |
| γ̇ | Gamma dot | Shear rate; subscript identifies the local gap or region |
| θ | Theta | Tangential direction, tangential velocity component, or stated geometric angle |