Basic Equations for Internal Compressible Flow: Assume: • Steady state, one-dimensional flow (or uniform flow and properties at all cross-sections) • Ideal gas with constant specific heats • Negligible body forces 2 flow Basic Equations for control volume from Section (1) to Section (2) of finite width and differential width, dx: Conservation of Mass Momentum Balance Conservation of Energy € Equation of State 2nd Law of Thermodynamics x heat transfer Finite Control Volume Differential Control Volume ρ1 V1 A1 = ρ2 V2 A2 dρ dV dA + + =0 ρ V A m˙ (V2 − V1 ) = p1 A1 − p2 A2 − pw ( A1 − A2 ) − Rx € € ⎛ V22 V12 ⎞ c p (T2 − T1 ) + ⎜ − ⎟ = qnet in 2 ⎠ ⎝ 2 € p1 p2 = ρ1 T1 ρ 2 T2 € € T ( s2 − s1 ) − qnet in ≥ 0 € Variables: Rx 1 Geometry € Net heat transfer per unit mass Net pressure on walls Reaction force due to friction Upstream flow conditions € Downstream flow conditions dV dp dRx =− 2 − V ρV ρV 2 A δqnet in dT dV 2 + = T 2c p T cp T dp dρ dT = + p ρ T T ds − δqnet in ≥ 0 € A1, A2 € qnet in = Q˙ net in m˙ pw Rx ρ1, p1, T1, V1 ρ 2 , p2 , T2 , V2 Problem Statement: given geometry, heat transfer rate, reaction force, and upstream flow € for downstream flow conditions. conditions for specified control volume, solve €
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