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)
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.
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.
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:
\(t_{min} = L/v_{max} = 28.6/5.050 = 5.663\ \text{s} = \boxed{0.0944\ \text{min}}\).
Decimal reduction time at process temperature. The z-value relation
\(D_T = D_{121}\, 10^{(121-T)/z}\) gives
\(D_{138} = 1.2 \times 10^{(121-138)/11} = 1.2 \times 10^{-1.545} = \boxed{0.0342\ \text{min}}\).
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
Quantity
Value
Flow regime
Laminar, \(Re \approx 916\)
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.