Dimensional at‐a‐station HG relations for (a) top width, (b) mean flow

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Dimensional at‐a‐station HG relations for (a) top width, (b) mean flow

Can the flow of a fluid stop due to friction with the pipe in a steady state? The velocity must stay constant so the pressure energy decreases instead, but will it ever

Dimensional at‐a‐station HG relations for (a) top width, (b) mean flow

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