| Quantity | Value | Notes |
|---|---|---|
| \(v_1=Q/A_1\), \(v_2=Q/A_2\), \(v_3=Q/A_3\) (m/s) | — | Bulk mean velocities at stations 1–3 |
| \(v_c = Q/(C_d A_2)\) (m/s) | — | “Effective jet” speed used in Clark’s Δp₁→₂ relation |
| \(\Delta p_{1\to2}\) (Pa / mmHg) | — | Across the stenosis; includes unsteady term \( \rho (dQ/dt)\beta_{12} \) |
| \(\Delta p_{2\to3}\) effective (Pa / mmHg) | — | Effective recovery = \(\Delta p_{1\to2}-\Delta p_{1\to3}^{(\mathrm{loss})}\) |
| \(\Delta p_{2\to3}\) quasi‑steady prediction (mmHg) | — | Borda–Carnot recovery (violet tick) |
| Non‑recoverable loss \(1\to3\) (Pa / mmHg) | — | Irreversible loss = nozzle + turbulent expansion (Clark loss model) |
| Unsteadiness index \(|\rho(dQ/dt)\beta_{12}|/|\Delta p_{1\to2,\mathrm{conv}}|\) (–) | — | Quasi‑steady is adequate when this is small |
| Area ratios \(A_2/A_1\), \(A_3/A_2\), \(A_2/A_3\) | — | Recovery prediction uses \(A_2/A_3\); loss uses \(A_3/A_2\) |
| Valve area estimate \(A_2\) (cm²) | — | Clark mean-data estimator: \(A_2 \simeq 0.0242\, \dfrac{\mathrm{CO}}{\sqrt{k\,\Delta p_{\text{mean}}}}\) |
Clark’s approach treats a stenosed valve as a nozzle-like constriction and evaluates discrete station pressures: upstream (1), at/just distal to the stenosis (2), and after mixing/recovery (3). The educational objective is to understand how \(C_d\), area ratios, and unsteadiness (\(dQ/dt\)) shape station-to-station pressure differences and pressure recovery in pulsatile flow.
\[ \Delta p_{1\to 2} \approx \frac{\rho}{2}\Big(\frac{Q}{C_d A_2}\Big)^2 \Big[1 - \Big(\frac{A_2}{A_1}\Big)^2\Big] \;+\; \rho\,\frac{dQ}{dt}\,\beta_{12}, \qquad \beta_{12}\approx \int_{1}^{2}\frac{dx}{A(x)}. \]
\[ \Delta p_{2\to 3}^{(\mathrm{qs})} \approx 2\Big(\frac{A_2}{A_3}\Big)\Big(1-\frac{A_2}{A_3}\Big)\,\frac{1}{2}\rho v_2^2, \qquad v_2=\frac{Q}{A_2}. \]
This value is displayed as the violet tick in the bar chart (prediction).
\[ \Delta p_{1\to 3}^{(\mathrm{loss})} = \frac{1}{2}\rho v_2^2 \left[ \Big(\frac{A_3}{A_2}\Big)^2\Big(1-\Big(\frac{A_2}{A_1}\Big)^2\Big)\Big(\frac{1}{C_d^2}-1\Big) +\Big(\frac{A_3}{A_2}-1\Big)^2 \right]. \]
\[ \Delta p_{2\to 3}^{(\mathrm{eff})} \;=\; \Delta p_{1\to2} \;-\; \Delta p_{1\to3}^{(\mathrm{loss})}. \]
The effective recovered pressure differs from the quasi‑steady prediction when nozzle/expansion losses are large and when the unsteady term shifts \(\Delta p_{1\to2}\).
\[ A_2 \simeq 0.0242\,\frac{\mathrm{CO}}{\sqrt{k\,\langle\Delta p\rangle}}\quad [\mathrm{cm}^2]. \]