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An engineer is to design an experimental apparatus that consists of a \(25-\mathrm{mm}\)-diameter smooth tube, where different fluids at \(100^{\circ} \mathrm{C}\) are to flow through in fully developed laminar flow conditions. For hydrodynamically and thermally fully developed laminar flow of water, engine oil, and liquid mercury, determine \((a)\) the minimum tube length and \((b)\) the required pumping power to overcome the pressure loss in the tube at largest allowable flow rate.

Short Answer

Expert verified
Answer: At a temperature of \(100^{\circ}\mathrm{C}\), the density and dynamic viscosity of water, engine oil, and liquid mercury are as follows: Water: - Density: \(\rho_{\text{Water}} = 958 \, \mathrm{kg/m^3}\) - Dynamic viscosity: \(\mu_{\text{Water}} = 2.82 \times 10^{-4} \, \mathrm{Pa \cdot s}\) Engine oil: - Density: \(\rho_{\text{Oil}} = 859 \, \mathrm{kg/m^3}\) - Dynamic viscosity: \(\mu_{\text{Oil}} = 7.17 \times 10^{-4} \, \mathrm{Pa \cdot s}\) Liquid mercury: - Density: \(\rho_{\text{Hg}} = 13534 \, \mathrm{kg/m^3}\) - Dynamic viscosity: \(\mu_{\text{Hg}} = 1.6 \times 10^{-3} \, \mathrm{Pa \cdot s}\)

Step by step solution

01

Determine fluid properties

For each fluid at a temperature of \(100^{\circ}\mathrm{C}\), we can find the density and dynamic viscosity values from the properties tables available in the literature. For water, engine oil, and liquid mercury, the values are as follows: Water: - Density: \(\rho_{\text{Water}} = 958 \, \mathrm{kg/m^3}\) - Dynamic viscosity: \(\mu_{\text{Water}} = 2.82 \times 10^{-4} \, \mathrm{Pa \cdot s}\) Engine oil: - Density: \(\rho_{\text{Oil}} = 859 \, \mathrm{kg/m^3}\) - Dynamic viscosity: \(\mu_{\text{Oil}} = 7.17 \times 10^{-4} \, \mathrm{Pa \cdot s}\) Liquid mercury: - Density: \(\rho_{\text{Hg}} = 13534 \, \mathrm{kg/m^3}\) - Dynamic viscosity: \(\mu_{\text{Hg}} = 1.6 \times 10^{-3} \, \mathrm{Pa \cdot s}\)
02

Confirm fully developed laminar flow

To confirm that the fluid flow is fully developed laminar, the Reynolds number should be less than 2000: $$\text{Re} = \frac{\rho vD}{\mu} < 2000$$ For each fluid, we will assume the largest allowable flow rate such that the above condition holds. Using the given tube diameter \(D=25\, \mathrm{mm}\), we can calculate the critical velocity for each fluid using the density and dynamic viscosity values we found in Step 1.
03

Determine the minimum tube length of each fluid

To determine the minimum tube length, first, we'll need to find the Nusselt number for each fluid. For laminar flow, it can be calculated using the following formula: $$\text{Nu} = 0.023 \; \text{Re}^{0.8}\, \text{Pr}^{n}$$ n = 0.4 for heating and 0.3 for cooling For this problem, let's assume the flow is cooled using a different analysis. Therefore, \(n\) will be 0.3. Next, we will calculate the Prandtl number, \(\text{Pr}\), for each fluid. Using the properties found in Step 1, we can calculate the specific heat at constant pressure, \(c_p\), for each fluid and thus finding the \(\text{Pr}\) using the formula: $$\text{Pr} = \frac{c_p\mu}{k}$$ Once we have the Prandtl number, we will determine the Nusselt number and find the ratios of entry lengths, \(L_{\text{entry}}\), for each fluid, and then find the minimum necessary value for each fluid.
04

Calculate required pumping power to overcome pressure loss

We will calculate the head loss for each fluid using the Hagen-Poiseuille equation in terms of pressure loss: $$\Delta P = \frac{128\mu QL}{\pi D^4}$$ Next, we will calculate the required pumping power, \(W\), and use the following formula for each fluid: $$W = \rho Q\Delta P$$ In conclusion, by following these steps and considering the properties of each fluid at the given temperature, we can determine the minimum tube length and required pumping power for fully developed laminar flow of water, engine oil, and liquid mercury.

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Key Concepts

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

Laminar Flow
In fluid dynamics, laminar flow describes a regime where fluid particles move in parallel paths, creating smooth and orderly layers. Unlike turbulent flow, where the fluid motion is chaotic, laminar flow is highly predictable and easy to model. It occurs at lower velocities and high fluid viscosity.
  • Characteristics: Fluid layers slide past one another with little to no mixing and disturbance between them.
  • Applications: Ideal for situations where precise, stable flow is needed, such as in chemical and biomedical engineering processes.
In the context of our problem, ensuring the flow remains laminar is crucial. It minimizes frictional losses in the tube, thereby reducing the effort needed to push the fluid through it. To ensure laminar flow, the velocity must be such that the Reynolds number remains below 2000.
Reynolds Number
The Reynolds number ( ext{Re}) is a dimensionless quantity used in fluid mechanics to determine whether fluid flow is laminar or turbulent. It is a ratio expressing the relative importance of inertial forces to viscous forces in the fluid's movement:
\[ ext{Re} = \frac{\rho vD}{\mu}\]
  • \( \rho \) is the fluid density
  • \( v \) is the velocity
  • \( D \) is the characteristic length (e.g., diameter of the tube)
  • \( \mu \) is the dynamic viscosity
For fully developed laminar flow in pipes, it is crucial that the Reynolds number is kept below 2000. This ensures that the flow maintains its orderly, laminar nature. In our problem, using given fluid properties, we can calculate the maximum velocity that keeps the flow laminar.
Hydrodynamic Entry Length
Hydrodynamic entry length refers to the distance a fluid must travel inside a pipe or tube before achieving a fully developed flow profile. Initially, as the fluid enters the pipe, it is influenced by the boundary and adjusts its velocity profile until it becomes steady.
  • Importance: The entry length affects calculations for pressure drop and heat transfer. It's pivotal in designing pipe systems efficiently.
  • Factors Influencing Length: Fluid properties and flow conditions such as Reynolds number.
In laminar flow, the hydrodynamic entry length can be estimated by:\[L_{entry} \approx 0.05 Re D\]By knowing this length, we can determine the minimum tube length required for maintaining consistent, fully developed flow.
Nusselt Number
The Nusselt number ( ext{Nu}) is a dimensionless quantity that indicates the enhancement of heat transfer through a fluid layer as a result of convection relative to conduction across the fluid layer. This ratio is crucial for evaluating heat transfer within fluids contained in tubes.
For our problem, the Nusselt number in laminar flows is determined using associated parameters through the equation:\[\text{Nu} = 0.023 Re^{0.8} Pr^n\]where \( Re \) is the Reynolds number, and \( Pr \) is the Prandtl number. The value of \( n \) differs based on cooling or heating conditions—here assumed to be 0.3 for cooling.
  • Role: Helps in calculating the heat transfer coefficient, augmenting design of thermal systems.
  • Calculation Consideration: Accounts for both velocity and thermal conductivities of the fluid and cylinder interaction.
Understanding the Nusselt number helps determine how effectively heat is transferred in the context of our exercise, providing insights into energy needed for fluid temperature control.

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Most popular questions from this chapter

Consider fully developed laminar flow in a circular pipe. If the diameter of the pipe is reduced by half while the flow rate and the pipe length are held constant, the pressure drop will \((a)\) double, \((b)\) triple, \((c)\) quadruple, \((d)\) increase by a factor of 8 , or \((e)\) increase by a factor of \(16 .\)

In a thermal system, water enters a \(25-\mathrm{mm}\)-diameter and \(23-\mathrm{m}\)-long circular tube with a mass flow rate of \(0.1 \mathrm{~kg} / \mathrm{s}\) at \(25^{\circ} \mathrm{C}\). The heat transfer from the tube surface to the water can be expressed in terms of heat flux as \(\dot{q}_{s}(x)=a x\). The coefficient \(a\) is \(400 \mathrm{~W} / \mathrm{m}^{3}\), and the axial distance from the tube inlet is \(x\) measured in meters. Determine \((a)\) an expression for the mean temperature \(T_{m}(x)\) of the water, \((b)\) the outlet mean temperature of the water, and \((c)\) the value of a uniform heat flux \(\dot{q}_{s}\) on the tube surface that would result in the same outlet mean temperature calculated in part (b). Evaluate water properties at \(35^{\circ} \mathrm{C}\).

The components of an electronic system dissipating \(180 \mathrm{~W}\) are located in a \(1-\mathrm{m}\)-long horizontal duct whose cross section is \(16 \mathrm{~cm} \times 16 \mathrm{~cm}\). The components in the duct are cooled by forced air, which enters at \(27^{\circ} \mathrm{C}\) at a rate of \(0.65 \mathrm{~m}^{3} / \mathrm{min}\). Assuming 85 percent of the heat generated inside is transferred to air flowing through the duct and the remaining 15 percent is lost through the outer surfaces of the duct, determine \((a)\) the exit temperature of air and \((b)\) the highest component surface temperature in the duct. As a first approximation assume flow is fully developed in the channel. Evaluate properties of air at a bulk mean temperature of \(35^{\circ} \mathrm{C}\). Is this a good assumption?

A computer cooled by a fan contains eight printed circuit boards (PCBs), each dissipating \(10 \mathrm{~W}\) of power. The height of the PCBs is \(12 \mathrm{~cm}\) and the length is \(18 \mathrm{~cm}\). The clearance between the tips of the components on the \(P C B\) and the back surface of the adjacent \(P C B\) is \(0.3 \mathrm{~cm}\). The cooling air is supplied by a 10 -W fan mounted at the inlet. If the temperature rise of air as it flows through the case of the computer is not to exceed \(10^{\circ} \mathrm{C}\), determine (a) the flow rate of the air that the fan needs to deliver, \((b)\) the fraction of the temperature rise of air that is due to the heat generated by the fan and its motor, and ( \(c\) ) the highest allowable inlet air temperature if the surface temperature of the components is not to exceed \(70^{\circ} \mathrm{C}\) anywhere in the system. As a first approximation, assume flow is fully developed in the channel. Evaluate properties of air at a bulk mean temperature of \(25^{\circ} \mathrm{C}\). Is this a good assumption?

Combustion gases passing through a 3-cm-internaldiameter circular tube are used to vaporize waste water at atmospheric pressure. Hot gases enter the tube at \(115 \mathrm{kPa}\) and \(250^{\circ} \mathrm{C}\) at a mean velocity of \(5 \mathrm{~m} / \mathrm{s}\), and leave at \(150^{\circ} \mathrm{C}\). If the average heat transfer coefficient is \(120 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and the inner surface temperature of the tube is \(110^{\circ} \mathrm{C}\), determine \((a)\) the tube length and (b) the rate of evaporation of water.

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