Hi every one~!!
Recently I am working on making 1-D simulation program for PF condensers performance. And I want to consider the effect of pressure dop in condenser performance.To do so, I approached to calculate tube-side pressure drop using Darcy's equation with f-smoth tube, turbulance. But calculations of pressure drop in Header side and in&out nozzles are confusing and challenging. For header side I found equation that is " K(G^2/2ρ)n=△P,n= number of tubes, K=1.6(two or more tubes side). is it applicable for condensers. I know I should apply two-phase pressure drop but I want to skip considering 2 phases for pressure drop calculation since I will use mean values of density and viscosity in 0-1 quality. the objective condenser has 5passes
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cingold (1); PWSlack (1); Sunwoo (1)