22-Agric-B8 Food Process Engineering (Part 1) · May 2014
Question 4 of 10: Sweet Cherry Freezing Time — Cleland-Earle Method
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 May 2014 — a three-hour open-book exam (any non-communicating calculator permitted). Ten questions are set in four sections (I–IV), each with a "do one/any N of M" instruction; a candidate following the choice rules answers 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, evaporator design — 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); R.P. Singh and D.R. Heldman, Introduction to Food Engineering, 5th ed. (freezing-time estimation, modified Plank and Cleland-Earle equations, 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).
Check: this paper's four roman-numeral section headers ("I. Heat transfer", "II. Food freezing and freeze concentration", "III. Thermal processing", "IV. Several assumptions (retort come-up correction factor, reference temperature for spore D-values, evaporator steam temperature reused for Question 9) are flagged inline where the source leaves a value implicit.
Find. Freezing time to -15°C by the Cleland-Earle method.
Approach. Cleland & Earle (1982) keep Plank's algebraic form but replace the fixed geometry fractions with regression functions of two dimensionless groups — the Plank number \(Pk\) (precooling sensible heat relative to \(\Delta H_1\)) and the Stefan number \(Ste\) (subcooling sensible heat relative to \(\Delta H_1\)) — so the geometry factors \(P,R\) are evaluated first, then substituted into the same Plank-style time equation used in Question 3.
Plank and Stefan numbers. \(Pk=\dfrac{C_{PU}(T_i-T_{fi})}{\Delta H_1}=\dfrac{0.22(5-(-2.5))}{278}=0.00594\); \(Ste=\dfrac{C_{PI}(T_{fi}-T_a)}{\Delta H_1}=\dfrac{2.05((-2.5)-(-30))}{278}=0.2028\).
Cleland-Earle geometry factors for a sphere. With \(E=3\) for a sphere, \(P=\dfrac{1}{2E}\big[1.026+0.5808\,Pk+Ste(0.2296\,Pk+0.1050)\big] = \boxed{0.1752}\) (vs. Plank's constant \(1/6=0.1667\)); \(R=\dfrac{1}{8E}\big[1.202+Ste(3.410\,Pk+0.7336)\big] = \boxed{0.0565}\) (vs. Plank's constant \(1/24=0.0417\)) — both correctly larger than the pure-Plank values, since the extra sensible-heat load increases the effective resistance term.
Check: the exam supplies no chart/table for the Cleland-Earle regression coefficients (unlike Fig. 1 for Question 1), so the standard published coefficients (Cleland & Earle, 1982, as reproduced in Toledo's Fundamentals of Food Process Engineering) are used directly; the small ~5-minute answer is physically reasonable given the cherry's small (1.5 cm) size and moderate \(h\).