The pressure difference (∆P) in a pipe of diameter (D) and length (L) due to viscous flow depends on the velocity of fluid (V), viscosity (µ) and density (ρ). Using Buckingham’s π theorem, show that ∆P=(µVL)/D² · f(Re) where Re=ρDV/μ is Reynold’s number.

Fluid Mechanics Problem Solution

Problem Statement

The pressure difference (∆P) in a pipe of diameter (D) and length (L) due to viscous flow depends on the velocity of fluid (V), viscosity (µ) and density (ρ). Using Buckingham’s π theorem, show that ∆P=(µVL)/D² · f(Re) where Re=ρDV/μ is Reynold’s number. (Take D, V and ρ as repeating variables)

Given Data

Variables Involved Pressure difference (∆P), Pipe diameter (D), Pipe length (L), Fluid velocity (V), Fluid viscosity (µ), Fluid density (ρ)
Repeating Variables D, V, and ρ
Total Number of Variables 6
Fundamental Dimensions 3 (M, L, T)
Expected Number of π Terms 6 – 3 = 3
To Prove ∆P=(µVL)/D² · f(Re) where Re=ρDV/μ

Solution Approach

To solve this problem, we’ll apply Buckingham’s π theorem, which states that a physical relationship between n variables that involve k fundamental dimensions can be rewritten as a relationship between (n-k) dimensionless π groups.

We have 6 variables and 3 fundamental dimensions, so we expect 3 dimensionless π groups. We’ll form these π groups using the repeating variables D, V, and ρ, and then manipulate them to obtain the required form.

Calculations

Dimensional Analysis

Step 1: Identify the dimensional formula for each variable:

Pressure difference (∆P) ML-1T-2
Pipe diameter (D) L
Pipe length (L) L
Fluid velocity (V) LT-1
Fluid viscosity (µ) ML-1T-1
Fluid density (ρ) ML-3

These dimensional formulas will be used to determine the exponents for each repeating variable in our π terms.

Step 2: Form the first π term with ∆P and the repeating variables:

π1 = Da1 · Vb1 · ρc1 · ∆P

For π1 to be dimensionless, we need:

[L]a1 · [LT-1]b1 · [ML-3]c1 · [ML-1T-2] = [M0L0T0]

Expanding and grouping by dimensions:

M: c1 + 1 = 0
L: a1 + b1 – 3c1 – 1 = 0
T: -b1 – 2 = 0

Solving the system of equations:

From T: b1 = -2
From M: c1 = -1
From L: a1 + (-2) – 3(-1) – 1 = 0
a1 – 2 + 3 – 1 = 0
a1 = 0

Therefore:

π1 = D0 · V-2 · ρ-1 · ∆P = ∆P / (ρV2)

Step 3: Form the second π term with L and the repeating variables:

π2 = Da2 · Vb2 · ρc2 · L

For π2 to be dimensionless, we need:

[L]a2 · [LT-1]b2 · [ML-3]c2 · [L] = [M0L0T0]

Expanding and grouping by dimensions:

M: c2 = 0
L: a2 + b2 – 3c2 + 1 = 0
T: -b2 = 0

Solving the system of equations:

From T: b2 = 0
From M: c2 = 0
From L: a2 + 0 – 0 + 1 = 0
a2 = -1

Therefore:

π2 = D-1 · V0 · ρ0 · L = L/D

Step 4: Form the third π term with μ and the repeating variables:

π3 = Da3 · Vb3 · ρc3 · μ

For π3 to be dimensionless, we need:

[L]a3 · [LT-1]b3 · [ML-3]c3 · [ML-1T-1] = [M0L0T0]

Expanding and grouping by dimensions:

M: c3 + 1 = 0
L: a3 + b3 – 3c3 – 1 = 0
T: -b3 – 1 = 0

Solving the system of equations:

From T: b3 = -1
From M: c3 = -1
From L: a3 + (-1) – 3(-1) – 1 = 0
a3 – 1 + 3 – 1 = 0
a3 = -1

Therefore:

π3 = D-1 · V-1 · ρ-1 · μ = μ/(ρDV)

We recognize that π3 = μ/(ρDV) = 1/Re, where Re is the Reynolds number.

Step 5: According to Buckingham’s π theorem, we can write:

f(π1, π2, π3) = 0

Or equivalently:

π1 = Φ(π2, π3)

Substituting our π terms:

∆P/(ρV2) = Φ(L/D, μ/(ρDV))

Step 6: To obtain the desired form ∆P=(µVL)/D² · f(Re), we manipulate the equation:

∆P/(ρV2) = Φ(L/D, μ/(ρDV))

Multiply both sides by ρV²:

∆P = ρV2 · Φ(L/D, μ/(ρDV))

Let’s rearrange the function to express it in terms of Re:

∆P = ρV2 · Φ(L/D, 1/Re)

We can rewrite this as:

∆P = ρV2 · (L/D) · Ψ(Re)

Where Ψ is a new function. Now we have:

∆P = ρV2 · (L/D) · Ψ(Re)

We can further manipulate this to get:

∆P = μV · (L/D²) · (ρDV/μ) · Ψ(Re)
∆P = (μVL/D²) · Re · Ψ(Re)

Define f(Re) = Re · Ψ(Re):

∆P = (μVL/D²) · f(Re)

∆P = (μVL/D²) · f(Re), where Re = ρDV/μ

Detailed Explanation

Significance of the Result

The result ∆P = (μVL/D²) · f(Re) is a general form of the pressure drop equation for pipe flow. It shows that:

  • Pressure drop is directly proportional to fluid viscosity (μ), velocity (V), and pipe length (L)
  • Pressure drop is inversely proportional to the square of pipe diameter (D²)
  • The function f(Re) accounts for the flow regime (laminar or turbulent) based on the Reynolds number

Special Cases

For fully developed laminar flow in a circular pipe, f(Re) = 64/Re, and the equation reduces to the Hagen-Poiseuille equation:

∆P = (μVL/D²) · (64/Re) = 64μ²VL/(ρD³V²) = 32μVL/D²

For turbulent flow, f(Re) is more complex and typically determined empirically using the Moody diagram or various friction factor correlations like Colebrook-White equation.

Applications in Engineering

This dimensional analysis result is fundamental in:

  • Designing piping systems for fluid transport
  • Sizing pumps based on pressure drop requirements
  • Analyzing flow control devices
  • Optimizing pipe networks for energy efficiency
  • Scale modeling and similarity analysis in fluid dynamics research

Power of Dimensional Analysis

This problem demonstrates the power of dimensional analysis and Buckingham’s π theorem in:

  • Reducing the number of variables in a complex physical problem
  • Identifying the key dimensionless groups that govern the phenomenon
  • Establishing general relationships without solving detailed differential equations
  • Facilitating experimental design and data correlation

Practical Implications

Understanding the pressure drop relationship has practical implications:

  • Doubling the pipe diameter reduces pressure drop by a factor of 16 (from the D² term)
  • Doubling the flow velocity increases pressure drop by at least a factor of 2 (more in turbulent flow)
  • Pressure drop scales linearly with pipe length
  • The transition from laminar to turbulent flow (governed by Re) significantly affects pressure drop behavior

This dimensional analysis approach provides a powerful framework for understanding and predicting fluid flow behavior in pipes without solving the complex Navier-Stokes equations directly.

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