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| \mu_w(T, p) = \mu_ |
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cdot (0.9994+4.0295\cdot 10^{-5} p + 3.1062 \cdot 10^{-9} p^2) |
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| \mu_{w, \, {\rm atm}}(T) = (109.574-8.40564 \, S+0.313314 \, S^2+8.72213 \cdot 10^{-5} \, S^3) \cdot T^{A} |
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| A=-1.2166 + 2.63951\cdot 10^{-2} \, S - 6.79461 \cdot 10^{-4} \, S^2 - 5.47119 \cdot 10^{-5} \, S^3 + 1.55586 \cdot 10^{-6} \, S^4 |
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| 2.547 · 10−4 bar-1 Temperature , K = 273 K ÷ 463 K | | 6.42 · 10−7 K−1 · bar-1 | Pressure, bar = 1 bar ÷ 800 bar | a_2 | 7.967 · 10−8 bar-2 | | Gas constant = 8.31446 · 10−3 kJ ⋅ mol−1 ⋅ K−1 | | 1.16 · 10−10 K−1 · bar-2 |
| 2.4055 ·10−2 cp| --uriencoded--\mu_%7Bw, \, %7B\rm atm%7D%7D(T) |
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2.795 · 10−4 kJ · mol−1 · bar-1b | 4.753 kJ · mol−1 | E | b_1 | 2.48 · 10−6 kJ · mol−1 · K−1 ·bar-1\theta | 139.7 K | | −4.85 · 10−3 K · bar-1c_1 | 6.32 · 10−5 bar-1
See Also
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Petroleum Industry / Upstream / Petroleum Engineering / Subsurface E&P Disciplines / Reservoir Engineering (RE) / PVT correlations / PVT Water correlations / Water viscosity correlations
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