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Oberbeck-Boussinesq approximation, for natural convection in porous media,2.11.5-1Oblate spheroids, free convective heat transfer from,2.5.7-25Ocean Thermal Energy Conversion (OTEC),3.22.3-1/3.22.3-20Octadecane:Octadecene:Octane:1-Octanol:1-Octene:Octafluorocyclobutane (Refrigerant C318)OEST, heat transfer medium,5.5.15-54Ohm (SI unit), xxviiiOldroyd eight constant model, for non-Newtonian fluid,2.2.8-9Olefins:Oliviera, S2.2.9-1/2.2.9-9, 2.5.16-1/2.5.16-5Olex, heat transfer medium,5.5.15-45ONB (onset of nucleate boiling):Once-through cooling towers,3.12.1-4Once-through multistage flash evaporators, (MSF-OT)One-equation models, for turbulent boundary layers,2.2.1-18Open-circuit cooling towers,3.12.1-4Openings, mechanical design aspects,4.1.8-1/4.1.8-2Operational envelope of a heat pipe,3.10.4-1Operational problems:Opposed convection:Optimization methods, for heat exchanger design,3.3.4-2Opto-microfluidics,2.5.11-11Organic compounds, aqueous solutions of, as heat transfer media,5.5.15-7/5.5.15-11Organic solids, density,5.4.1-2Organic sulfur compounds:Organic vapours, dropwise condensation of,2.6.5-8/2.6.5-9Orifices:Orifice baffles, in tube bundles with longitudinal flow,3.3.12-6O-ring seal, hollow metal,4.14.8-1Orrick and Erbar method for saturated liquid viscosity,5.1.4-6/5.1.4-15OTEC, (see Ocean Thermal Energy Conversion)OTL (see Outer tube limit)Outer tube limit, in shell-and-tube heat exchangers,4.2.5-9Outlet effects, in shell-and-tube heat exchangers,3.3.6-9/3.3.6-10Overall heat transfer coefficient,2.1.2-1Overall power hypothesis, for critical heat flux in flow boiling,2.7.3-24Overcapacity, in condensers,3.4.5-1/3.4.5-2Oxygen:
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