SUPERFICIE SCALDATA
UNITA’ DI MISURA DESCRIZIONE
α W·m-2·K-1 coefficiente di scambio termico
β K-1 dT dρ ρ 1 −
= coefficiente di dilatazione cubica
βτ K-1 dT dε ε 1 −
= coefficiente di temperatura della permettività elettrica
γ V·m-1 rigidità dielettrica
δt m altezza dello strato limite termico
ε F·m-1 permettività del mezzo
εbulk - errore percentuale sulla temperatura del bagno
εd/Lc - errore percentuale sulla distanza tra gli elettrodo εI - errore percentuale sulla stima della corrente del
circuito di bassa tensione
εL - errore percentuale sulla stima dell’area di misura εM - errore percentuale del modulo di acquisizione εNu - errore percentuale sul numero di Nusselt
εq - errore percentuale sul flusso termico della lastra εR - errore percentuale sulla resistenza della lastra εRC - errore percentuale della resistenza campione εRTD - errore percentuale della termoresisteza εS - errore percentuale dello strumento εT K errore assoluto sulla temperatura εT% - errore percentuale sulla temperatura
εV - errore percentuale sulla tensione ai capi della
lastra
εVC - errore percentuale sulla lettura del potenziale ai
capi della resistenza campione.
ε∆T - errore percentuale sul salto di temperatura tra
fluido e parete
ζMAX m raggio dei siti attivi di nucleazione della bolla λD m lunghezza d’onda di Taylor
λH m lunghezza d’onda del getto instabile µ Kg⋅ m-1⋅ s-1 viscosità dinamica
ν m2·s-1 viscosità cinematica
ρ kg·m-3 densità di massa
E
ρ C·m-3 densità di carica caratteristica
L kg·m-3 densità del liquido ρV kg·m-3 densità del vapore σ N⋅ m-1 tensione superficiale
σE S·m-1 conducibilità elettrica
σST Ω deviazione standard (resistenza)
τ Pa tensore degli sforzi viscosi
χ parametro definito nell’equazione (1.12)
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NUMERO ADIMENSIONALE DESCRIZIONE
Bo numero di Bond E* γ ⋅ ⋅ ⋅ = r z r HV 2 ln Ja numero di Jacob Ja* fg bulk P h T T Cp⋅( − ) = Ja** fg SAT P h T T Cp⋅( − ) = K numero di Kutateladze M parametro di mobilità Nu numero di Nusselt Pr numero di Prandtl Re numero di reynolds
145
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