22-Agric-B8 Food Process Engineering (Part 1) · May 2014
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
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).
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.
| Quantity | Symbol | Value |
|---|---|---|
| Diameter (treated as infinite cylinder) | \(D\) | 4 cm → \(a=2\) cm |
| Surface coefficient | \(h\) | 20 W/(m²·K) |
| Initial temperature | \(T_i\) | 2°C |
| Air (medium) temperature | \(T_a\) | -20°C |
| Initial freezing point | \(T_{fi}\) | -2°C |
| Target centre temperature | \(T_{f}\) | -10°C |
| Latent heat of fusion of water | \(\Delta H_{fus}\) | 333 kJ/kg |
| Moisture content | — | 90% |
| Frozen-phase conductivity | \(k_I\) | 1.108 W/(m·K) |
| Frozen-phase specific heat | \(C_{PI}\) | 2.05 kJ/(kg·K) |
| Unfrozen-phase specific heat | \(C_{PU}\) | 4.22 kJ/(kg·K) |
| Density | \(\rho\) | 1000 kg/m³ |
Find. The freezing time to reach a centre temperature of -10°C, using the Levy-modified Plank equation.
Approach. The stated \(\Delta H\) is the water-fusion latent heat, not a true sublimation term, so it is used to build the total volumetric enthalpy change the product must give up: sensible heat above the freezing point (precooling to \(T_{fi}\)), the phase-change latent heat scaled by the moisture fraction, and sensible heat below the freezing point (subcooling the frozen phase down to the -10°C target). That combined \(\Delta H_{tot}\) replaces the pure latent heat in Plank's original cylinder equation.
| Quantity | Value |
|---|---|
| \(\Delta H_f\) (latent, per kg product) | 299.7 kJ/kg |
| \(\Delta H_{tot}\) (precool+latent+subcool) | 333.0 kJ/kg |
| Freezing time \(t\) | 84.0 min (1.40 h) |