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Oblate spheroids, free convective heat transfer from, Ocean Thermal Energy Conversion (OTEC), Octadecane: Octadecene: Octane: 1-Octanol: 1-Octene: Octafluorocyclobutane (Refrigerant C318) OEST, heat transfer medium, Oldroyd eight constant model, for non-Newtonian fluid, Olefins: Oliviera, S Olex, heat transfer medium, ONB (onset of nucleate boiling): Once-through cooling towers, Once-through multistage flash evaporators, (MSF-OT) One-equation models, for turbulent boundary layers, Open-circuit cooling towers, Operational envelope of a heat pipe, Operational problems: Opposed convection: Opto-microfluidics, Organic compounds, aqueous solutions of, as heat transfer media, Organic solids, density,
Density of Solids
Organic sulfur compounds: Organic vapours, dropwise condensation of, Orifices: Orifice baffles, in tube bundles with longitudinal flow, Orrick and Erbar method for saturated liquid viscosity, Outer tube limit, in shell-and-tube heat exchangers, Outlet effects, in shell-and-tube heat exchangers, Overall heat transfer coefficient, Overall power hypothesis, for critical heat flux in flow boiling, Overcapacity, in condensers, Oxygen:

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HEDH
A B C D E F G H I J K L M N O
Oblate spheroids, free convective heat transfer from, Ocean Thermal Energy Conversion (OTEC), Octadecane: Octadecene: Octane: 1-Octanol: 1-Octene: Octafluorocyclobutane (Refrigerant C318) OEST, heat transfer medium, Oldroyd eight constant model, for non-Newtonian fluid, Olefins: Oliviera, S Olex, heat transfer medium, ONB (onset of nucleate boiling): Once-through cooling towers, Once-through multistage flash evaporators, (MSF-OT) One-equation models, for turbulent boundary layers, Open-circuit cooling towers, Operational envelope of a heat pipe, Operational problems: Opposed convection: Opto-microfluidics, Organic compounds, aqueous solutions of, as heat transfer media, Organic solids, density,
Density of Solids
Organic sulfur compounds: Organic vapours, dropwise condensation of, Orifices: Orifice baffles, in tube bundles with longitudinal flow, Orrick and Erbar method for saturated liquid viscosity, Outer tube limit, in shell-and-tube heat exchangers, Outlet effects, in shell-and-tube heat exchangers, Overall heat transfer coefficient, Overall power hypothesis, for critical heat flux in flow boiling, Overcapacity, in condensers, Oxygen:
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O Organic solids, density,
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Density of Solids

DOI 10.1615/hedhme.a.000518

5.4 PROPERTIES OF SOLIDS
5.4.1 Density of solids

M. Schunck

For a material with unknown density (i.e., mass per unit volume, ρ, in kg/m3 rarely more than the simplest facts will be available. Thus these have to be taken as the basis for deriving an estimated density.

A. Metal alloys

The densities of the pure metals are related to their places in the Periodic table but are not strictly parallel to their atomic masses. The density of alloys can be estimated as the composed density according to the mass fractions of the single elements in the alloy:

\[\label{eq1} \rho_A=\dfrac1{x_1/\rho_1+x_2/\rho_2+x_3/\rho_3} \tag{1}\]

where ρi is the density of the single component and ρA the density of the alloy.

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