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Where Kf is the thermal conductivity of the fluid, pco is plate corrugation pitch, Dh is hydraulic diameter, x is quality of fluid entering the condenser, ρf and ρg are the density of saturated liquid and vapor at condenser inlet condition. Here we need to observe that the Reynolds number (Re) is based on hydraulic diameter. REFERENCE: [1] Muley, A., Manglik, R. M., “Experimental Study of Turbulent Flow Heat Transfer and Pressure Drop in a Plate Heat Exchanger with Chevron Angle”, ASME Journal of Heat Transfer, February 1999, Vol.121, pp.110–117. [2] Ayub, Z. H., “Plate Heat Exchanger Literature Survey and New Heat Transfer and Pressure Drop Correlations for Refrigerant Evaporators”, Journal of Heat Transfer Engineering, 2003, Vol.25 (5), pp.3–16. [3] Selvam, M. A. J., Senthil, K. P., Muthuraman, S., “The Characteristics of Brazed Plate Heat Exchangers with Different Chevron Angles”, ARPN Journal of Engineering and Applied Sciences, December 2009, Vol. 4 (10), pp.19–26. 85PDF Image | Optimizing Heat Recovery Systems for Power Generation in Rural AK
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