Reference flow states

h_{o} = h + \frac{1}{2} u^{2} \Rightarrow C p T_{o} = C_{p} T + \frac{1}{2} u^{2} \Rightarrow \frac{T_{o}}{T} = 1 + \frac{1}{2 C_{p}} M^{2} γ R T = 1 + \frac{γ - 1}{2} M^{2}

(Eq. 3.1)

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