ICAR AICE-JRF/SRF (PhD) — Food Processing Technology, Food Safety & Quality, Processing and Food Engineering · India · ICAR through the National Testing Agency
Original practice questions written to the published syllabus · not past papersThe mechanical operations that clean, sort, reduce, mix, homogenise and separate food materials, including filtration, centrifugation and membrane processes, with the design equations used to size them.
In the exams: GATE XE-G Section 4 (mechanical operations); ICAR AIEEA-PG Code 18 Unit II (cleaning, sorting, size reduction, mixing, separation, filtration, membranes)
ICAR AICE-JRF/SRF (PhD) — Food Processing Technology, Food Safety & Quality, Processing and Food Engineering
35.a Unit 5 covers unit operations of grading, sorting, peeling and size reduction; 37 Unit 4 covers membrane processing; 41 covers post-harvest unit operations, process machinery design and material handling. Expect deeper questions on membrane fouling and diafiltration, compressible cakes, centrifuge sigma theory and supercritical extraction.
How our questions for ICAR AICE-JRF/SRF spread across the units of Mechanical Unit Operations: Size Reduction, Mixing & Separation. Difficulty: 0 easy, 43 medium, 22 hard.
| Mixing of solids, pastes and liquids; agitation and power number | 6 | |
| Centrifugation and centrifugal separators | 6 | |
| Membrane processes: microfiltration, ultrafiltration, nanofiltration and reverse osmosis | 6 | |
| Sieving and particle-size analysis | 5 | |
| Filtration: cake filtration theory and filter aids | 5 | |
| Crystallisation | 5 | |
| Distillation and supercritical fluid extraction | 5 | |
| Size-reduction equipment for dry and wet foods | 4 | |
| High-pressure homogenisation | 4 | |
| Expression and solid-liquid extraction | 4 | |
| Cleaning, sorting and grading of raw materials | 3 | |
| Peeling methods | 3 | |
| Size reduction: energy laws of Rittinger, Kick and Bond | 3 | |
| Settling and sedimentation | 3 | |
| Material handling: conveyors and elevators for foods | 3 |
Choose an answer, then open the working. Each explanation says why the right answer is right and why the others are not.
Compared with abrasion peeling, flash steam peeling generally gives
D. lower losses and less effluent
Abrasion peeling rubs off flesh with the skin and needs much water; steam peeling is efficient with little effluent.
Further reading: Fellows, Food Processing Technology
A sample contains 3 particles of 10 µm, 2 of 20 µm and 1 of 30 µm. Its Sauter mean diameter d32 is closest to
A. 23.0 µm
d32 = (3×1,000 + 2×8,000 + 27,000)/(3×100 + 2×400 + 900) = 46,000/2,000 = 23.0 µm. 16.7 is the number mean; 20.0 is d21; 25.2 is d43.
Further reading: McCabe, Smith and Harriott, Unit Operations of Chemical Engineering
Laser diffraction particle sizing differs from sieve analysis in that it
D. gives volume-based distributions with fine resolution below 50 µm
Laser diffraction converts light-scattering patterns to volume distributions; methods measure different properties and give different results.
Further reading: McCabe, Smith and Harriott, Unit Operations of Chemical Engineering
The capacity of a gravity settling tank to remove particles of a given size depends mainly on its
D. surface area
A particle is removed if its settling velocity exceeds flow/surface area (overflow rate), so area, not depth, governs capacity.
Further reading: Geankoplis, Transport Processes and Separation Process Principles
In reverse osmosis, transmembrane pressure is 4.0 MPa, osmotic pressure difference 2.0 MPa, permeate viscosity 0.001 Pa s and total resistance 2 × 10¹³ m⁻¹. Using J = (ΔP − Δπ)/(μRt), the flux is closest to
C. 360 L/m² h
J = 2.0 × 10⁶/(10⁻³ × 2 × 10¹³) = 1.0 × 10⁻⁴ m/s = 360 L/m² h. 720 ignores osmotic pressure; 0.10 is per second; 1080 adds osmotic pressure.
Further reading: Cheryan, Ultrafiltration and Microfiltration Handbook
Diafiltration in whey protein production means
A. adding water to the retentate and filtering again to wash out lactose and salts
Diluting and re-filtering removes permeable components, raising protein purity, as in whey protein isolates.
Further reading: Cheryan, Ultrafiltration and Microfiltration Handbook
Reverse osmosis cannot concentrate fruit juice much beyond about 25–30 % solids mainly because
D. osmotic pressure rises with concentration and opposes the applied pressure
π = icRT grows with solute concentration, so very high pressures would be needed; RO is used to pre-concentrate.
Further reading: Cheryan, Ultrafiltration and Microfiltration Handbook
100 kg of water saturated with lactose at 60 °C (solubility 59 g per 100 g water) is cooled to 20 °C (solubility 19 g per 100 g water). Ignoring water of crystallisation, the lactose that can crystallise is about
D. 40 kg
59 − 19 = 40 kg. 19 kg remains dissolved; 59 kg is the total; 78 adds the two.
Further reading: McCabe, Smith and Harriott, Unit Operations of Chemical Engineering
High supersaturation during crystallisation tends to produce
D. many small crystals
High supersaturation favours nucleation over growth.
Further reading: McCabe, Smith and Harriott, Unit Operations of Chemical Engineering
Small amounts of ethanol are added as a co-solvent to supercritical CO₂ mainly to
C. extend extraction to more polar compounds
CO₂ is non-polar; ethanol increases its ability to dissolve polar compounds.
Further reading: McCabe, Smith and Harriott, Unit Operations of Chemical Engineering
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