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 extruder as a continuous cooker and shaper: single- and twin-screw extruders, the transformations of starch and protein inside them, expanded snacks, breakfast cereals, pasta, and high-moisture extrusion for meat analogues.
In the exams: GATE XE-G Section 3 (extruded products, ready-to-eat breakfast cereals); ICAR AIEEA-PG Code 18 Unit II (extrusion)
ICAR AICE-JRF/SRF (PhD) — Food Processing Technology, Food Safety & Quality, Processing and Food Engineering
35.a Unit 2 names extruded products, breakfast and snack foods and texturised vegetable proteins; 41 covers process technology and machinery. Expect deeper questions on screw configuration, SME, RTD, starch fragmentation, high-moisture extrusion and co-extrusion.
How our questions for ICAR AICE-JRF/SRF spread across the units of Extrusion & Texturisation Technology. Difficulty: 9 easy, 35 medium, 23 hard.
| Single-screw extruders: flow and pressure | 8 | |
| Twin-screw extruders: configuration and screw elements | 7 | |
| Die design and product shaping | 7 | |
| Starch transformations during extrusion | 7 | |
| Protein texturisation: low-moisture and high-moisture extrusion | 7 | |
| Specific mechanical energy and process variables | 6 | |
| Pasta and cold-forming extrusion | 6 | |
| Quality evaluation of extrudates: expansion ratio and bulk density | 6 | |
| Expanded snacks and ready-to-eat breakfast cereals | 5 | |
| Co-extrusion and filled products | 5 | |
| Principles of extrusion cooking | 3 |
Choose an answer, then open the working. Each explanation says why the right answer is right and why the others are not.
A screw with D = 0.08 m turns at 2 rev/s with helix angle 17.7°; the channel is 0.06 m wide and 0.006 m deep. Using Qd = ½VzWH with Vz = πDN cos θ, the drag flow is closest to
B. 0.31 m³/h
Vz = π × 0.08 × 2 × cos 17.7° = 0.479 m/s; Qd = ½ × 0.479 × 0.06 × 0.006 = 8.62e-05 m³/s = 0.31 m³/h. Doubling omits the ½; omitting cos θ gives 0.33; the last leaves the value in m³/s.
Further reading: Harper, Extrusion of Foods
Grooved barrels are used in single-screw food extruders to
A. prevent slip at the barrel wall
If material slips and turns with the screw, conveying fails; grooves grip it.
Further reading: Harper, Extrusion of Foods
Using a die with smaller openings on the same extruder generally
B. raises die pressure and lowers output
A more restrictive die shifts the operating point along the screw characteristic.
Further reading: Harper, Extrusion of Foods
Food twin-screw extruders commonly have length-to-diameter ratios of about
D. 20–40
L/D of roughly 20–40 allows feeding, cooking, venting and pressurising zones.
Further reading: Guy (ed.), Extrusion Cooking: Technologies and Applications
Vitamins are usually added to extruded cereals
A. after extrusion, by spraying or coating
Thiamin, vitamin C and folate are heat-sensitive and lost in the extruder.
Further reading: Fast and Caldwell, Breakfast Cereals and How They Are Made
A meat analogue needs 45 N to cut perpendicular to its fibres and 15 N parallel to them. Its anisotropy index is
B. 3.0
45/15 = 3.0; values above 1 indicate fibrousness. 0.33 inverts; 30 subtracts; 60 adds.
Further reading: Riaz (ed.), Extruders in Food Applications
Switching to a different supplier's pea protein changes meat-analogue texture markedly. The best response is to
A. specify protein functionality and re-run extrusion trials
Protein solubility and gelling vary between ingredients; specifications and trials keep texture consistent.
Further reading: Riaz (ed.), Extruders in Food Applications
Halving the radius of a circular die opening, other things equal, raises the die pressure drop by a factor of
C. 16
ΔP ∝ 1/R⁴; halving R multiplies ΔP by 2⁴ = 16.
Further reading: Harper, Extrusion of Foods
Phase separation between protein-rich and water- or polysaccharide-rich phases in high-moisture extrusion is thought to
B. contribute to the layered, fibrous structure
Separated phases are elongated in the cooling die, adding anisotropy.
Further reading: Riaz (ed.), Extruders in Food Applications
Dried pasta is dried to a final moisture of about
D. 12 %
Drying from about 30 % to about 12 % or below gives a stable product.
Further reading: Kill and Turnbull, Pasta and Semolina Technology
Ten here, 67 in the app. The Laisha app has every practice question we have written to ICAR AICE-JRF/SRF in this subject, marked as you go, with timed papers, a jump-to-unanswered list and a certificate when you pass at 70 per cent.
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