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(1) \mu_w(T, p) = \mu_{w1} \cdot  (0.9994+4.0295\cdot 10^{-5} p + 3.1062 \cdot 10^{-9} p^2)
(2) \mu_{w1}(T) = (109.574-8.40564 \, S+0.313314 \, S^2+8.72213 \cdot 10^{-5} \, S^3) \cdot T^{A}
(3) 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



\mu_w 

Dynamic viscositycp

a

2.547 · 104 bar-1

T 

Temperature , K = 273 K ÷ 463 K

a_1

6.42 · 107 K−1 · bar-1

p 

Pressure, bar = 1 bar ÷ 800 bar

a_2

7.967 · 108 bar-2

R 

Gas constant8.31446 · 103 kJ ⋅ mol−1 ⋅ K−1

a_3

1.16 · 1010 K−1 · bar-2

\mu_0 

2.4055 ·102 cp

b

2.795 · 104 kJ · mol−1 · bar-1

E

4.753 kJ · mol−1 

b_1

2.48 · 106 kJ · mol−1 · K−1 ·bar-1

\theta

139.K

c

4.85 · 103 K · bar-1

S

water salinity

c_1

6.32 · 105 bar-1


See Also


Petroleum Industry / Upstream / Petroleum Engineering / Subsurface E&P Disciplines / Reservoir Engineering (RE) / PVT correlations / PVT Water correlations / Water viscosity correlations



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