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Vasiliev, L,
Vassilicos, J C,
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Vertical cylindrical fired heater,
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Visco-elastic fluids, flow of,
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liquid, effect on critical heat flux in pool boiling,
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of multicomponent mixtures,
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of pure fluids
gases,
liquids,
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of superheated gases,
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of water,
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Index
HEDH
A
B
C
D
E
F
G
H
I
J
K
L
M
N
O
P
Q
R
S
T
U
V
Vacuum equipment, operational problems of,
Vacuum operation, of reboilers,
Valle, A,
Valves:
Vaned bends, single-phase flow and pressure drop in,
Vapor blanketing, as mechanism of critical heat flux,
Vapor injection, effect of on boiling heat transfer in tube bundles,
Vapor-liquid disengagement, in kettle reboilers,
Vapor-liquid separation, for evaporators,
Vapor mixtures, condensation of,
Vapor pressure,
Vapor recompression, in evaporation,
Vaporization, choice of evaporator type for,
Vaporizer, double bundle, constructional features,
Vapors, saturation properties of,
Vapors, properties of superheated,
Vasiliev, L,
Vassilicos, J C,
Velocity defect law:
Velocity distribution:
Velocity fluctuations, in turbulent pipe flow,
Velocity ratio (slip ratio):
Venting of condensers
Vertical condensers:
Vertical cylindrical fired heater,
Vertical pipes:
Vertical surfaces:
Vertical thermosiphon reboilers:
Vessels of non-circular cross section, design to ASME VIII code,
Vessels of rectangular cross section, EN13445 guidance for,
Vetere method, for enthalpy of vaporisation,
Vibrated beds, heat transfer to,
Vibration:
Vinyl acetate:
Vinyl benzene:
Vinyl chloride:
Virial equation:
Virk equation for maximum drag reduction,
Visco-elastic fluids, flow of,
Viscometric functions (non-Newtonian flow), methods of determining,
Viscosity:
W
X
Y
Z
of emulsions,
of fluids at elevated pressure,
of heat transfer media,
of heavy water,
liquid, effect on critical heat flux in pool boiling,
of liquid water,
of liquids below their boiling point,
of multicomponent mixtures,
non-Newtonian,
of pure fluids
gases,
liquids,
relation with density for gases,
of supercritical fluids,
of saturated liquids and vapors,
of seawater,
small variations in,
of superheated gases,
variation with temperature:
of water,
Viscosity number (Vi),
Viscous dissipation, influence on heat transfer in non-Newtonian flows,
Viscous heat generation, in scraped sauce heat exchangers,
Viscous sublayer, in duct flow,
Void fraction,
Voidage, in fixed beds, definition,
Volumetric heat transfer coefficient,
Volumetric mass transfer coefficient,
von Karman friction factor equation for fully rough surface,
von Karman velocity defect law,
Vortex flow, in helical coils of rectangular cross section,
Vortex flow model, for twisted tube heat exchangers,
Vortex shedding:
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Properties of Liquid Heavy Water
DOI 10.1615/hedhme.a.000532
5.5 PHYSICAL PROPERTY DATA TABLES
5.5.9 Properties of liquid heavy water
G. Ulrych
Critical properties: pc = 216.59 bar; Tc = 370.66 °C; Tc = 643.81 K; ρc = 350 kg/m3; molecular weight: Ṁ = 20.028 kg/kmol; triple point: Tt = 3.82 °C.
Table 1 Properties of liquid heavy water at p = 1 bar a,b
a T, temperature; ρ, density; cp specific heat capacity; β, thermal expansion coefficient; λ, thermal conductivity; η, dynamic viscosity; ν, kinematic viscosity; κ, thermal diffusivity; Pr, Prandtl number. b Properties according to Nagashima and Matsunaga (1979) and Hill et al. (1981). |
||||||||
T, °C | ρ, kg/m3 | cp, kJ/kg K | β, 10–3/K | λ, 10–3 W/m K | η, 10–3 kg/m s | ν, 10–6 m2/s | κ, 10–6 m2/s | Pr |
---|---|---|---|---|---|---|---|---|
3.82 | 1,105.5 | 4.210 | –0.132 | 564 | 2,058 | 1.861 | 0.121 | 15.35 |
10.00 | 1,106.0 | 4.231 | –0.027 | 570 | 1,689 | 1.527 | 0.122 | 12.53 |
20.00 | 1,105.4 | 4.242 | 0.121 | 580 | 1,253 | 1.133 | 0.124 | 9.17 |
30.00 | 1,103.3 | 4.240 | 0.242 | 589 | 972 | 0.881 | 0.126 | 7.00 |
40.00 | 1,100.0 | 4.232 | 0.343 | 597 | 785 | 0.713 | 0.128 | 5.56 |
50.00 | 1,095.7 | 4.220 | 0.428 | 605 | 648 | 0.591 | 0.131 | 4.52 |
60.00 | 1,090.6 | 4.207 | 0.502 | 611 | 545 | 0.500 | 0.133 | 3.75 |
70.00 | 1,084.7 | 4.194 | 0.569 | 617 | 468 | 0.432 | 0.136 | 3.18 |
80.00 | 1,078.2 | 4.181 | 0.631 | 621 | 409 | 0.379 | 0.138 | 2.75 |
90.00 | 1,071.0 | 4.170 | 0.689 | 625 | 363 | 0.339 | 0.140 | 2.42 |
Table 2 Density ρ of liquid heavy water as a function of pressure and temperature a
a ρ in kg/m3. | |||||||||
Pressure, bar | Temperature, °C | ||||||||
---|---|---|---|---|---|---|---|---|---|
3.82 | 20 | 50 | 100 | 150 | 200 | 250 | 300 | 350 | |
1 | 1,105.5 | 1,105.4 | 1,095.7 | 1,063.4 | |||||
10 | 1,106.0 | 1,105.9 | 1,096.1 | 1,063.8 | 1,017.6 | ||||
50 | 1,108.3 | 1,108.0 | 1,098.1 | 1,065.9 | 1,020.1 | 961.2 | 885.1 | ||
100 | 1,111.1 | 1,110.6 | 1,100.5 | 1,068.5 | 1,023.2 | 965.3 | 891.5 | 788.3 | |
150 | 1,113.9 | 1,113.1 | 1,102.9 | 1,071.0 | 1,026.3 | 969.4 | 897.5 | 800.3 | |
170 | 1,115.0 | 1,114.1 | 1,103.9 | 1,072.0 | 1,027.5 | 970.9 | 899.9 | 804.7 | 625.8 |
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