NivaarExam PrepOfficial exam papers ↗

22-Mec-B6 Advanced Fluid Mechanics · May 2016

Question 5 of 6: Buckingham Pi analysis of a sudden contraction

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

Paper format. National Exams, May 2016 — 07-Mec-B6 Advanced Fluid Mechanics. Three hours, OPEN BOOK, any approved Sharp or Casio calculator permitted. Six questions are printed; any five of them constitute a complete paper, each carries an equal 20 marks, and the item weights are shown in the left margin. No aid sheet is bound into this paper — the open-book rule is the candidate’s table source, so every compressible-flow ratio below is quoted in closed form rather than read off a chart. All six questions are solved here.

Reference texts. Solutions follow the conventions of the texts the EGBC syllabus recommends for this subject:

Question 5: Buckingham Pi analysis of a sudden contraction (20 marks)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

Given. The functional statement Δp = f(D1, D2, U, ρ, μ), where U is the velocity in the larger pipe, with D1, U and μ nominated as the repeating variables.

Find. A complete, independent set of dimensionless groups, and a reasoned explanation of why the velocity in the smaller pipe must not be added to the variable list.

Sudden contraction: the pressure drop is measured across the stepUseparation / vena contractapressure drop across the contractionD₁D₂
The sudden contraction. The pressure drop is measured between a tap upstream in the large pipe and one downstream in the small pipe, beyond the vena contracta where the jet has refilled the bore.

Approach. Count variables and independent dimensions to fix the number of groups, confirm the nominated repeating set is dimensionally independent, then solve one small linear system per non-repeating variable.

  1. Count. The variable list is Δp, D1, D2, U, ρ, μ, so n = 6. In the MLT system their dimensions are $$[\Delta p]=ML^{-1}T^{-2},\quad [D_{1}]=[D_{2}]=L,\quad [U]=LT^{-1}, \quad [\rho]=ML^{-3},\quad [\mu]=ML^{-1}T^{-1},$$ and the rank of the dimensional matrix is k = 3. Buckingham’s theorem therefore predicts $$n-k=6-3=3\ \text{dimensionless groups}.$$
  2. Confirm the nominated repeating variables are admissible. The set {D1, U, μ} must be dimensionally independent and must not by itself form a dimensionless group. Mass appears only in μ, time only in U and μ, and length in all three, and no product D1aUbμc is dimensionless unless a = b = c = 0. The set is valid, and note in passing that it deliberately excludes the dependent variable Δp, as the method requires.
  3. First group: the dependent variable. Seek Π1 = Δp D1aUbμc. Balancing exponents, $$M:\ 1+c=0,\qquad T:\ -2-b-c=0,\qquad L:\ -1+a+b-c=0,$$ which gives c = −1, b = −1, a = 1, so $$\boxed{\;\Pi_{1}=\frac{\Delta p\,D_{1}}{\mu U}\;}$$ a viscous-scaled pressure drop — the natural form when viscosity is a repeating variable.
  4. Second group: the geometry. With Π2 = D2D1aUbμc, the mass balance gives c = 0, the time balance b = 0, and the length balance a = −1: $$\boxed{\;\Pi_{2}=\frac{D_{2}}{D_{1}}\;}$$ the contraction ratio, which is the only geometric parameter the problem contains.
  5. Third group: the remaining property. With Π3 = ρD1aUbμc, $$M:\ 1+c=0,\qquad T:\ -b-c=0,\qquad L:\ -3+a+b-c=0,$$ giving c = −1, b = 1, a = 1, so $$\boxed{\;\Pi_{3}=\frac{\rho U D_{1}}{\mu}=\mathrm{Re}_{D_{1}}\;}$$ the Reynolds number based on the upstream pipe.
  6. State the result. The dimensionless statement of the problem is $$\frac{\Delta p\,D_{1}}{\mu U}=\phi\!\left(\frac{D_{2}}{D_{1}},\ \mathrm{Re}_{D_{1}}\right),$$ a reduction from a function of five variables to a function of two. Any independent recombination is equally valid, and the one used in practice divides out the viscosity: $$\frac{\Pi_{1}}{\Pi_{3}}=\frac{\Delta p}{\rho U^{2}}=\mathrm{Eu} =\phi'\!\left(\frac{D_{2}}{D_{1}},\ \mathrm{Re}_{D_{1}}\right),$$ the Euler number, which is preferred because at high Reynolds number the loss coefficient becomes almost independent of Re and collapses onto a single curve in D2/D1. A worked instance: with Δp = 4.2 kPa, D1 = 0.20 m, D2 = 0.10 m, U = 3 m/s and water, Π1 = 2.79 × 105, Π2 = 0.5, Π3 = 5.98 × 105 and Eu = 0.468.
  7. Part (b) — why the small-pipe velocity must be excluded. The velocity in the smaller pipe is not an independent quantity. Conservation of mass for an incompressible fluid fixes it completely from variables already on the list: $$U_{2}=U\left(\frac{D_{1}}{D_{2}}\right)^{2},\qquad\text{i.e.}\qquad \frac{U_{2}}{U}=\Pi_{2}^{-2}.$$ Buckingham’s theorem requires the variable list to be independent; a quantity that is an algebraic function of others is redundant.
  8. What actually goes wrong if you add it. Adding U2 raises n to 7 while the rank stays at k = 3, so the method dutifully produces a fourth group, U2D22/(UD12). But that group is identically equal to unity for every physically realisable flow: it is not a free parameter, it is a constraint the fluid has already satisfied. Carrying it forward is misleading in two ways. It suggests the problem has one more degree of freedom than it does, so an experimenter might waste a whole test matrix trying to vary it independently; and it breaks the uniqueness of the correlation, because the same physical state can now be labelled by infinitely many nominally different parameter sets. The rule generalises: include the independent variables that define the problem, and let the conservation laws supply everything they determine.
PartGroupFormName
(a)Π1Δp D1 / (μU)viscous-scaled pressure drop
(a)Π2D2 / D1contraction ratio
(a)Π3ρU D1 / μReynolds number
(a)ResultΠ1 = φ(Π2, Π3)equivalently Eu = Δp/ρU2 = φ′(Π2, Re)
(b)ReasonU2 = U(D1/D2)2not independent — fixed by continuity; yields a group identically equal to 1