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Kandlikar correlation, for forced convective boiling,
Katto and Ohne correlation, for critical heat flux in forced convective boiling,
Kaunas correlation, for heat transfer in staggered high fin tube banks,
Kern method, for shell-side heat transfer in shell-and-tube heat exchangers,
Kern-Seaton model for fouling,
Taborek modification of,
Ketene:
Ketones:
Kettle reboilers:
Kilger, H-J,
Kinematic viscosity:
Kirchoff's law, in radiative heat transfer,
Klincewicz and Reid correlations:
Knudsen, Jmes G
Kopp and Sayre method for pressure design of expansion bellows,
Koslov, A,
Kreglewski and Kay method for critical pressure of mixtures,
Krypton:
Kumar, H
Index
HEDH
A
B
C
D
E
F
G
H
I
J
K
Kandlikar correlation, for forced convective boiling,
Katto and Ohne correlation, for critical heat flux in forced convective boiling,
Kaunas correlation, for heat transfer in staggered high fin tube banks,
Kern method, for shell-side heat transfer in shell-and-tube heat exchangers,
Kern-Seaton model for fouling,
Taborek modification of,
Ketene:
Ketones:
Kettle reboilers:
Kilger, H-J,
Kinematic viscosity:
Kirchoff's law, in radiative heat transfer,
Klincewicz and Reid correlations:
Knudsen, Jmes G
Kopp and Sayre method for pressure design of expansion bellows,
Koslov, A,
Kreglewski and Kay method for critical pressure of mixtures,
Krypton:
Kumar, H
L
M
N
O
P
Q
R
S
T
U
V
W
X
Y
Z
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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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