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Engine oil at \(105^{\circ} \mathrm{C}\) flows over the surface of a flat plate whose temperature is \(15^{\circ} \mathrm{C}\) with a velocity of \(1.5 \mathrm{~m} / \mathrm{s}\). The local drag force per unit surface area \(0.8 \mathrm{~m}\) from the leading edge of the plate is (a) \(21.8 \mathrm{~N} / \mathrm{m}^{2}\) (b) \(14.3 \mathrm{~N} / \mathrm{m}^{2}\) (c) \(10.9 \mathrm{~N} / \mathrm{m}^{2}\) (d) \(8.5 \mathrm{~N} / \mathrm{m}^{2}\) (e) \(5.5 \mathrm{~N} / \mathrm{m}^{2}\) (For oil, use \(\nu=8.565 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}, \rho=864 \mathrm{~kg} / \mathrm{m}^{3}\) )

Short Answer

Expert verified
Answer: The local drag force per unit surface area is approximately 10.9 N/m².

Step by step solution

01

Calculate the Reynolds number at the given location

To calculate the Reynolds number at \(0.8\mathrm{~m}\) from the leading edge of the plate, we use the formula: \(Re=\frac{Vx}{\nu}\), where \(V=1.5\mathrm{~m} / \mathrm{s}\) is the velocity of the oil, \(x=0.8\mathrm{~m}\) is the distance from the leading edge, and \(\nu=8.565\times10^{-5}\mathrm{~m}^{2}/\mathrm{s}\) is the kinematic viscosity of the oil. $$Re=\frac{(1.5\mathrm{~m/s})(0.8\mathrm{~m})}{8.565\times10^{-5}\mathrm{~m}^{2}/\mathrm{s}}\approx 14,067$$
02

Use the Blasius equation to find the local drag coefficient \(C_f\)

The Blasius equation for the local drag coefficient of a flat plate in a laminar flow is: \(C_f=\frac{0.664}{Re^{1/2}}\). Using the calculated Reynolds number from Step 1: $$C_f=\frac{0.664}{\sqrt{14,067}}\approx0.005618$$
03

Calculate the local drag force per unit surface area

To find the local drag force per unit area, we use the drag force formula: \(F =\frac{1}{2}\rho V^2 C_f\). Here, \(\rho=864\mathrm{~kg} / \mathrm{m}^{3}\) is the density of the oil. Substituting the values, we get: $$F =\frac{1}{2}(864\mathrm{~kg/m}^{3})(1.5\mathrm{~m/s})^2(0.005618) \approx 10.89\mathrm{~N/m}^{2}$$ Thus, the local drag force per unit surface area at the given location is approximately \(10.9\mathrm{~N/m}^{2}\) which corresponds to option (c).

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Reynolds Number
The Reynolds number is a crucial dimensionless parameter used in fluid mechanics to determine the flow characteristics of a fluid. It helps to predict the transition from laminar to turbulent flow. The formula to calculate the Reynolds number \(Re\) is given by:\[Re = \frac{Vx}{u}\]where:
  • \(V\) is the velocity of the fluid (\(1.5\ \mathrm{m/s}\) in this case).

  • \(x\) is the characteristic length (the specific location from the leading edge, \(0.8\ \mathrm{m}\)).

  • \(u\) is the kinematic viscosity of the fluid (\(8.565\times10^{-5}\ \mathrm{m}^2/\mathrm{s}\)).
Substituting the values, the Reynolds number was found as approximately \(14067\). A value of the Reynolds number under 2300 typically indicates laminar flow, while a value over 4000 would suggest turbulent flow. However, in this scenario, since the plate is flat and it's a transitional phase, the flow can still be considered laminar despite a higher number.
Blasius Equation
The Blasius equation is an empirical relationship used to determine the local drag coefficient for laminar flow over a flat plate. The equation is derived from the boundary layer theory and is expressed as:\[C_f = \frac{0.664}{Re^{1/2}}\]Here, \(C_f\) represents the local drag coefficient. It is a measure that indicates the drag force experienced by a flat surface due to the fluid flow.
By substituting the previously calculated Reynolds number \(14067\) into the Blasius equation, we get:
  • \(C_f = \frac{0.664}{\sqrt{14067}} \approx 0.005618\)
This calculates the resistance that the fluid encounters while flowing over the plate. It helps in understanding how streamlined an object needs to be to minimize the frictional effects of the fluid.
Local Drag Coefficient
The local drag coefficient \(C_f\) is a key factor in determining the drag force acting on a surface in contact with a fluid flow. It provides an indication of how much resistance the surface encounters due to the fluid's movement. The drag force per unit area \(F\) is calculated using the formula:\[F = \frac{1}{2} \rho V^2 C_f\]where:
  • \(\rho\) represents the fluid density (here, \(864\ \mathrm{kg/m^3}\)).

  • \(V\) is the velocity (\(1.5\ \mathrm{m/s}\)).

  • \(C_f\) is the local drag coefficient (calculated as \(0.005618\)).
By substituting the appropriate values, the drag force per unit surface area was calculated to be approximately \(10.9\ \mathrm{N/m}^2\). This highlights how the choice of surface material and fluid properties can affect the drag experienced by an object.
Kinematic Viscosity
Kinematic viscosity is a measure of a fluid's internal resistance to flow. It describes how easily a fluid flows under the influence of gravity and is typically denoted by \(u\). Kinematic viscosity is calculated by dividing the dynamic viscosity by the density of the fluid. For this problem, the engine oil has a kinematic viscosity of:\[u = 8.565 \times 10^{-5} \ \mathrm{m}^2/\mathrm{s}\]This parameter plays a crucial role in influencing the Reynolds number calculation. A fluid with higher kinematic viscosity would flow more slowly and have a smaller Reynolds number under the same conditions. Conversely, a lower viscosity means easier flow and a potentially larger Reynolds number. Understanding kinematic viscosity helps engineers and scientists in designing and analyzing systems involving fluid dynamics.

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Most popular questions from this chapter

A heated long cylindrical rod is placed in a cross flow of air at \(20^{\circ} \mathrm{C}(1 \mathrm{~atm})\) with velocity of \(10 \mathrm{~m} / \mathrm{s}\). The rod has a diameter of \(5 \mathrm{~mm}\) and its surface has an emissivity of \(0.95\). If the surrounding temperature is \(20^{\circ} \mathrm{C}\) and the heat flux dissipated from the rod is \(16000 \mathrm{~W} / \mathrm{m}^{2}\), determine the surface temperature of the rod. Evaluate the air properties at \(70^{\circ} \mathrm{C}\).

During a plant visit, it was noticed that a 12-m-long section of a \(10-\mathrm{cm}\)-diameter steam pipe is completely exposed to the ambient air. The temperature measurements indicate that the average temperature of the outer surface of the steam pipe is \(75^{\circ} \mathrm{C}\) when the ambient temperature is \(5^{\circ} \mathrm{C}\). There are also light winds in the area at \(10 \mathrm{~km} / \mathrm{h}\). The emissivity of the outer surface of the pipe is \(0.8\), and the average temperature of the surfaces surrounding the pipe, including the sky, is estimated to be \(0^{\circ} \mathrm{C}\). Determine the amount of heat lost from the steam during a 10 -h-long work day. Steam is supplied by a gas-fired steam generator that has an efficiency of 80 percent, and the plant pays \(\$ 1.05 /\) therm of natural gas. If the pipe is insulated and 90 percent of the heat loss is saved, determine the amount of money this facility will save a year as a result of insulating the steam pipes. Assume the plant operates every day of the year for \(10 \mathrm{~h}\). State your assumptions.

During flow over a given body, the drag force, the upstream velocity, and the fluid density are measured. Explain how you would determine the drag coefficient. What area would you use in calculations?

Liquid mercury at \(250^{\circ} \mathrm{C}\) is flowing with a velocity of \(0.3 \mathrm{~m} / \mathrm{s}\) in parallel over a \(0.1-\mathrm{m}\)-long flat plate where there is an unheated starting length of \(5 \mathrm{~cm}\). The heated section of the flat plate is maintained at a constant temperature of \(50^{\circ} \mathrm{C}\). Determine \((a)\) the local convection heat transfer coefficient at the trailing edge, \((b)\) the average convection heat transfer coefficient for the heated section, and \((c)\) the rate of heat transfer per unit width for the heated section.

Air at 1 atm and \(20^{\circ} \mathrm{C}\) is flowing over the top surface of a \(0.5-\mathrm{m}\)-long thin flat plate. The air stream velocity is \(50 \mathrm{~m} / \mathrm{s}\) and the plate is maintained at a constant surface temperature of \(180^{\circ} \mathrm{C}\). Determine \((a)\) the average friction coefficient, \((b)\) the average convection heat transfer coefficient, and (c) repeat part (b) using the modified Reynolds analogy.

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