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Algebraic equations such as Bernoulli's relation, Eq. (1) of Ex. \(1.3,\) are dimensionally consistent, but what about differential equations? Consider, for example, the boundary-layer \(x\) -momentum equation, first derived by Ludwig Prandtl in 1904 : $$\rho u \frac{\partial u}{\partial x}+\rho v \frac{\partial u}{\partial y}=-\frac{\partial p}{\partial x}+\rho g_{x}+\frac{\partial \tau}{\partial y}$$ where \(\tau\) is the boundary-layer shear stress and \(g_{x}\) is the component of gravity in the \(x\) direction. Is this equation dimensionally consistent? Can you draw a general conclusion?

Short Answer

Expert verified
The boundary-layer equation is dimensionally consistent.

Step by step solution

01

Examine the Terms

For the given boundary-layer equation, list all the terms: \(\rho u \frac{\partial u}{\partial x} + \rho v \frac{\partial u}{\partial y} = -\frac{\partial p}{\partial x} + \rho g_x + \frac{\partial \tau}{\partial y}\). Each term must have the same dimensions to be dimensionally consistent.
02

Find Dimensions of Each Term

Calculate the dimensions of each term. \(\rho u \frac{\partial u}{\partial x}\) has dimensions \([ML^{-2}T^{-2}]\), \(\rho v \frac{\partial u}{\partial y}\) has \([ML^{-2}T^{-2}]\), \(-\frac{\partial p}{\partial x}\) has \([ML^{-2}T^{-2}]\), \(\rho g_x\) has \([ML^{-2}T^{-2}]\), and \(\frac{\partial \tau}{\partial y}\) has \([ML^{-2}T^{-2}]\).
03

Compare Dimensions

Check if all terms on both sides of the equation have the same dimensions. Each term has dimensions \([ML^{-2}T^{-2}]\), confirming that the equation is dimensionally consistent.
04

Draw General Conclusion

Since all terms have consistent dimensions, we can generalize that for a differential equation to be dimensionally consistent, each term must represent the same physical dimensions. This ensures physical validity across each part of the equation.

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Key Concepts

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

Boundary-Layer Theory
Boundary-layer theory is a fundamental concept in fluid dynamics. It helps us understand the behavior of fluid flow near surfaces, like the air movement over an airplane wing or water along a ship's hull. Ludwid Prandtl introduced this theory in 1904, revolutionizing our approach to analyzing viscous flow.

At the heart of boundary-layer theory lies the concept of the boundary layer itself. This is a thin layer of fluid, right next to a solid surface, where the effects of viscosity are most significant. In this layer, fluid velocity changes from zero at the surface to approximately free-stream velocity further away.

  • Boundary-layer thickness is the distance across the layer where fluid velocity has adjusted to about 99% of the free-stream velocity.
  • Understanding the boundary-layer allows engineers to predict drag forces on objects, enhancing design efficiency.
The boundary-layer concept is crucial for solving complex problems involving fluid dynamics and helps simplify equations describing fluid movement by focusing on the significant viscous effects in this narrow region.
Momentum Equation
In fluid dynamics, the momentum equation is key to understanding how forces change fluid motion. It's part of the broader set of equations known as the Navier-Stokes equations, which describe the motion of viscous fluid substances.

The momentum equation involves various parameters:
  • Velocity (\(u\) and \(v\)) of the fluid in different directions.
  • Pressure (\(p\)) differences across the fluid.
  • External forces like gravity (\(g_x\)).
  • Shear stress (\(\tau\)) due to fluid viscosity.
For boundary-layer problems, these terms are crucial as they define how the fluid flows past surfaces. To achieve dimensional consistency, as in the given boundary-layer momentum equation, every term must share the same units: mass (M), length (L), and time (T). This ensures the equation's physical validity and that each calculation represents the same fundamental behaviors in fluid dynamics.
Prandtl's Boundary Layer
Prandtl's boundary layer concept narrowed down fluid analysis to the most significant region affecting fluid flow: right along the boundary. It made fluid dynamics more approachable for practical applications.

By introducing this layer, Prandtl showed that a separate analysis of the boundary layer could significantly simplify solving the equations of motion for fluid flow. Within this layer:
  • Viscous forces are comparable to inertia forces, unlike in the free stream.
  • The boundary-layer equations assume the flow outside the boundary layer is essentially non-viscous, reducing complexity.
Analyzing Prandtl's boundary layer helps identify where disturbances to flow patterns mainly occur and highlights areas needing attention for managing drag or flow separation. Thus, in engineering applications, utilizing Prandtl's insights allows for more efficient design choices, optimizing structures to better manage fluid interactions across surfaces.

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Most popular questions from this chapter

The efficiency \(\eta\) of a pump is defined as the (dimensionless) ratio of the power developed by the flow to the power required to drive the pump: $$\eta=\frac{Q \Delta p}{\text { input power }}$$ where \(Q\) is the volume rate of flow and \(\Delta p\) is the pressure rise produced by the pump. Suppose that a certain pump develops a pressure rise of 35 lbf/in \(^{2}\) when its flow rate is \(40 \mathrm{L} / \mathrm{s} .\) If the input power is \(16 \mathrm{hp},\) what is the efficiency?

Yaws et al. [34] suggest the following curve-fit formula for viscosity versus temperature of organic liquids: $$\log _{10} \mu \approx A+\frac{B}{T}+C T+D T^{2}$$ with \(T\) in absolute units. (a) Can this formula be criticized on dimensional grounds? ( \(b\) ) Disregarding \((a)\), indicate analytically how the curve-fit constants \(A, B, C, D\) could be found from \(N\) data points \(\left(\mu_{i}, T_{i}\right)\) using the method of least squares. Do not actually carry out a calculation.

The kinematic viscosity of a fluid is the ratio of viscosity to density, \(\nu=\mu / \rho .\) What is the only possible dimensionless group combining \(\nu\) with velocity \(V\) and length \(L ?\) What is the name of this grouping? (More information on this will be given in Chap. 5.)

The Stokes-Oseen formula [18] for drag force \(F\) on a sphere of diameter \(D\) in a fluid stream of low velocity \(V\) density \(\rho,\) and viscosity \(\mu,\) is $$F=3 \pi \mu D V+\frac{9 \pi}{16} \rho V^{2} D^{2}$$ Is this formula dimensionally homogeneous?

Do some reading and report to the class on the life and achievements, especially vis-à -vis fluid mechanics, of (a) Evangelista Torricelli \((1608-1647)\) (b) Henri de Pitot \((1695-1771)\) \((c)\) Antoine Chézy \((1718-1798)\) \((d)\) Gotthilf Heinrich Ludwig Hagen \((1797-1884)\) \((e)\) Julius Weisbach \((1806-1871)\) \((f)\) George Gabriel Stokes \((1819-1903)\) \((g)\) Moritz Weber \((1871-1951)\) (h) Theodor von Kármán ( \(1881-1963\) ) (i) Paul Richard Heinrich Blasius \((1883-1970)\) (j) Ludwig Prandtl (1875-1953) (k) Osborne Reynolds \((1842-1912)\) ( \(l\) ) John William Strutt, Lord Rayleigh \((1842-1919)\) \((m)\) Daniel Bernoulli \((1700-1782)\) \((n)\) Leonhard Euler \((1707-1783)\).

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