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22-Agric-A6 Physical Properties of Biological Materials and Food Products · May 2015

Question 5 of 9: Freezing vs. Thawing Rate Asymmetry; Shape Effects on Heating Rate

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

Notes on this paper

Paper format. 04-Agric-A6 Physical Properties of Biological Materials and Food Products, National Exams May 2015 — a three-hour closed-book exam (approved calculator permitted; one aid sheet, both sides). Nine questions are set and candidates answer any five, each worth 20 marks, for a 100-mark paper. All nine are worked here so the set is a complete study resource.

Reference texts. M.A. Rao, S.S.H. Rizvi, A.K. Datta and J. Ahmed, Engineering Properties of Foods, 4th ed. (rheology of fluid and semisolid foods, particle size, optical and dielectric properties); N.N. Mohsenin, Physical Properties of Plant and Animal Materials, 2nd ed. (thermal and rheological properties of biological materials, surface heat transfer coefficient measurement, stress relaxation); R.P. Singh and D.R. Heldman, Introduction to Food Engineering, 5th ed. (freezing/thawing rates and shape factors, unsteady-state heat transfer, screen analysis); J.F. Steffe, Rheological Methods in Food Process Engineering, 2nd ed. (viscoelasticity, generalized Maxwell model, time-dependent flow behaviour); R.L. Earle, Unit Operations in Food Processing, 2nd ed. (specific surface and particle number from sieve/screen data).

Question 5: Freezing vs. Thawing Rate Asymmetry; Shape Effects on Heating Rate (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.

Part (a) — freezing is faster than thawing. During freezing, heat is removed through a growing outer layer of ice; during thawing of the same product, heat must be conducted inward through a growing outer layer of thawed (liquid) material to reach the still-frozen core. Ice's thermal conductivity is roughly four times that of liquid water (kice ≈ 2.2 W/m·K vs. kwater ≈ 0.6 W/m·K), so in freezing the resistance of the growing outer layer that heat must cross stays comparatively low throughout the process, while in thawing the growing outer layer has the low- conductivity phase, and its thermal resistance grows steadily as thawing proceeds — the process self-decelerates. In addition, industrial freezing is typically carried out with a large driving temperature difference (a freezer or blast-freezing medium tens of degrees below 0°C), while thawing is usually carried out at or only modestly above ambient/refrigeration temperatures (both for food-safety reasons — a large thawing ΔT would overheat and spoil the already- thawed outer layer long before the centre thaws), so the driving force itself is smaller for thawing as well. Both effects point the same way, so a product that freezes in, say, an hour can easily take several hours to thaw.

Part (b) — shape and heating rate. For the same characteristic dimension (the half-thickness L of the slab equal to the radius R of the cylinder and the sphere), the sphere heats fastest, the infinite cylinder is intermediate, and the infinite slab heats slowest. The physical reason is that heat enters a sphere from every direction simultaneously and converges toward a shrinking centre, whereas a cylinder is heated from all radial directions in a plane but not from the ends (treated as infinite), and a slab is heated from only one pair of parallel faces (one-dimensional conduction) — the more directions from which heat can reach the interior for the same characteristic length, the faster the centre responds. This can be seen quantitatively from each shape's volume-to-surface-area ratio, which sets its lumped-system time constant τ = ρVc/(hA) (or, for internal-gradient-limited heating, its Fourier-solution eigenvalue): for a slab of half-thickness L, V/A = L; for a cylinder of radius R, V/A = R/2; for a sphere of radius R, V/A = R/3. With L = R, the ratio of time constants is therefore slab : cylinder : sphere = 1 : 1/2 : 1/3 — the sphere's characteristic response time is one-third that of the slab, and the cylinder's is one-half that of the slab, for the identical characteristic dimension.