Suppose that the fluid being sheared in Fig. 1.8 is SAE 30 oil at 20°C. Compute the shear stress in the oil if V = 3 m/s and h = 2 cm.
Suppose that the fluid being sheared in Fig. 1.8 is SAE 30 oil at 20°C. Compute the shear stress in the oil if V = 3 m/s and h = 2 cm.
• System sketch: This is shown earlier in Fig. 1.8.
• Assumptions: Linear velocity profile, laminar newtonian fluid, no slip at either plate surface.
• Approach: The analysis of Fig. 1.8 leads to Eq. (1.26) for laminar flow.
u = V \frac{y}{h} (1.26)
• Property values: From Table 1.4 for SAE 30 oil, the oil viscosity µ = 0.29 kg/(m-s).
Table 1.4 Viscosity and Kinematic Viscosity of Eight Fluids at 1 atm and 20°C | |||||
Fluid | µ, kg/(m·s)^† |
Ratio µ/µ(H_2) |
ρ, kg/m^3 |
v, m^2/s^† |
Ratio v/v(Hg) |
Hydrogen | 9.0 E-6 | 1.0 | 0.084 | 1.05 E-4 | 910 |
Air | 1.8 E-5 | 2.1 | 1.20 | 1.50 E-5 | 130 |
Gasoline | 2.9 E-4 | 33 | 680 | 4.22 E-7 | 3.7 |
Water | 1.0 E-3 | 114 | 998 | 1.01 E-6 | 8.7 |
Ethyl alcohol | 1.2 E-3 | 135 | 789 | 1.52 E-6 | 13 |
Mercury | 1.5 E-3 | 170 | 13,550 | 1.16 E-7 | 1.0 |
SAE 30 oil | 0.29 | 33,000 | 891 | 3.25 E-4 | 2,850 |
Glycerin | 1.5 | 170,000 | 1,260 | 1.18 E-3 | 10,300 |
^†1 kg/(m·s) = 0.0209 slug/(ft·s); 1 m^2/s = 10.76 ft^2/s.
• Solution steps: In Eq. (1.26), the only unknown is the fluid shear stress:
\tau = µ\frac{V}{h} = \left(0.29\frac{kg}{m \cdot s}\right) \frac{(3 m/s)}{(0.02 m)} = 43.5 \frac{kg \cdot m/s^2}{m^2} = 43.5\frac{N}{m^2} \approx 44 Pa Ans.
• Comments: Note the unit identities, 1 kg-m/s^2 ≡ 1 N and 1 N/m^2 ≡ 1 Pa. Although oil is very viscous, this shear stress is modest, about 2400 times less than atmospheric pressure. Viscous stresses in gases and thin (watery) liquids are even smaller.