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22-Agric-B8 Food Process Engineering (Part 1) · December 2013

Question 1 of 10: Aseptic Holding-Tube Spoilage Probability

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

Notes on this paper

Paper format. 04-Agric-B8 Food Process Engineering (Part 1), National Exams December 2013 — a three-hour open-book exam (any non-communicating calculator permitted). Ten questions are set in four sections (I–IV), each with a "choose N of M" instruction; candidates who follow the choice rule answer six questions for a 100-mark paper. All ten are worked here so the set is a complete study resource.

Reference texts. R.T. Toledo, Fundamentals of Food Process Engineering, 3rd ed. (thermal-process lethality, D and z values, Ball/Stumbo process calculation, aseptic holding-tube residence time — this is the exam's own appendix source); C.J. Geankoplis, Transport Processes and Separation Process Principles, 4th ed. (evaporator heat and mass balances, multiple-effect steam economy, vapour recompression); R.P. Singh and D.R. Heldman, Introduction to Food Engineering, 5th ed. (freezing-time estimation, modified Plank equation, unsteady-state heat transfer in canned foods); A.C. Cleland, Food Refrigeration Processes: Analysis, Design and Simulation (Plank/Cleland-Earle freezing-time correlations); F.P. Incropera and D.P. DeWitt, Fundamentals of Heat and Mass Transfer (transient conduction, Heisler charts, composite-wall resistance).

Question 1: Aseptic Holding-Tube Spoilage Probability (15 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.

Holding-tube and thermal-resistance data
QuantitySymbolValue
Tube length\(L\)28.6 m
Pipe inside diameter\(d\)3.48 cm = 0.0348 m
Volumetric flow rate\(Q\)144.1 L/min
Density\(\rho\)1042 kg/m³
Viscosity\(\mu\)100 cP = 0.100 Pa·s
Process temperature\(T\)138°C
z-value\(z\)11°C
Reference decimal reduction time\(D_{121}\)1.2 min
Initial spore load\(N_0\)100 spores/can

Find. The probability of spoilage (surviving-spore fraction) delivered by this holding tube.

Approach. Confirm the flow regime, take the residence time of the fastest-moving fluid element (not the mean) as the process time since that particle sees the least lethal treatment, convert \(D_{121}\) to \(D_{138}\) via the z-value, and apply the survivor-ratio (Bigelow) equation.

  1. Mean velocity and Reynolds number. \(A = \dfrac{\pi}{4}d^2 = \dfrac{\pi}{4}(0.0348\ \text{m})^2 = 9.511\times10^{-4}\ \text{m}^2\). \(\bar v = Q/A = \dfrac{144.1\times10^{-3}/60\ \text{m}^3/\text{s}}{9.511\times10^{-4}\ \text{m}^2} = 2.525\ \text{m/s}\). \(Re = \dfrac{\rho \bar v d}{\mu} = \dfrac{1042 \times 2.525 \times 0.0348}{0.100} \approx 916\) — below 2100, so the flow is laminar.
  2. Fastest-particle residence time. For laminar Newtonian flow the parabolic profile gives a centreline (maximum) velocity of \(v_{max} = 2\bar v = 5.050\ \text{m/s}\). Aseptic-process design uses the minimum residence time, since that is the time seen by the least-treated element: \(t_{min} = L/v_{max} = 28.6/5.050 = 5.663\ \text{s} = \boxed{0.0944\ \text{min}}\).
  3. Decimal reduction time at process temperature. The z-value relation \(D_T = D_{121}\, 10^{(121-T)/z}\) gives \(D_{138} = 1.2 \times 10^{(121-138)/11} = 1.2 \times 10^{-1.545} = \boxed{0.0342\ \text{min}}\).
  4. Survivor ratio and spoilage probability. The Bigelow lethality equation \(\log_{10}(N_0/N) = t/D_T\) gives a log-reduction of \(t_{min}/D_{138} = 0.0944/0.0342 = 2.762\), so \(N = N_0\, 10^{-2.762} = 100\times1.731\times10^{-3} = \boxed{0.173\ \text{spores/can}}\). Because \(N<1\), this value is read directly as the fraction of cans expected to contain a surviving spore.
Final results
QuantityValue
Flow regimeLaminar, \(Re \approx 916\)
Fastest-particle residence time, \(t_{min}\)5.66 s (0.0944 min)
\(D_{138}\)0.0342 min
Probability of spoilage\(\approx 0.173\) (17.3%)
Check: this holding tube / flow-rate combination does not achieve commercial sterility (spoilage risk far above the industry target of < \(10^{-9}\)); the numbers are taken exactly as given rather than adjusted, since the exam's evident intent is to test whether the candidate recognises an under-designed process.
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