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GATE Evaporation, Dehydration & Concentration of Foods: practice questions

GATE — Life Sciences (XL), Section U Food Technology · India · IITs and IISc on rotation (2026: IIT Guwahati)

Original practice questions written to the published syllabus · not past papers
10worked here, free
72written to this exam in this subject
13syllabus units

What this subject covers

Removing water from liquid and solid foods: evaporator types and energy economy, drying theory and dryer design, spray, drum and freeze drying, concentration by freezing and membranes, and the quality changes that drying causes. Agricultural Engineering's post-harvest-cereals-pulses-oilseeds covers grain drying; this subject covers processed foods and powders.

In the exams: GATE XE-G Section 4 (evaporation, hot-air drying, spray and freeze drying, psychrometry); ICAR AIEEA-PG Code 18 Units II–III

What GATE asks from it

GATE — Engineering Sciences (XE), Section G Food Technology

Section 4 names evaporation of liquid foods, hot-air drying of solids, spray and freeze drying, and psychrometry, humidification and dehumidification; Section 3 names dehydration and intermediate-moisture foods. Expect numericals on humidity ratio and enthalpy of air, air-flow requirements, evaporator mass balance and steam economy, moisture-basis conversion and constant- and falling-rate drying times, plus reasoning on dryer and evaporator selection.

GATE — Life Sciences (XL), Section U Food Technology

Same Section 3–4 content as XE-G. Questions tend to link drying to water activity, browning and microbial stability, as well as the standard moisture-basis and psychrometric calculations.

Where the 72 questions fall

How our questions for GATE spread across the units of Evaporation, Dehydration & Concentration of Foods. Difficulty: 18 easy, 45 medium, 9 hard.

Psychrometry, humidification and dehumidification8
Drying theory: constant-rate and falling-rate periods8
Evaporation: boiling-point elevation and heat transfer7
Single- and multiple-effect evaporators; steam economy7
Spray drying: atomisation, powder properties and agglomeration6
Freeze drying: principles, cycle design and collapse temperature6
Hot-air dryers: cabinet, tunnel, belt and fluidised-bed5
Osmotic dehydration and intermediate-moisture foods5
Freeze concentration and membrane concentration5
Quality changes in dried foods and rehydration5
Falling-film, forced-circulation and plate evaporators4
Vapour recompression: thermal and mechanical3
Drum drying3

10 practice questions, worked

Choose an answer, then open the working. Each explanation says why the right answer is right and why the others are not.

1 · Psychrometry, humidification and dehumidification · medium

As air passes over wet food in an adiabatic dryer, its state follows approximately a line of constant

  1. wet-bulb temperature
  2. dry-bulb temperature
  3. humidity ratio
  4. relative humidity
Answer and working

A. wet-bulb temperature

Heat for evaporation comes from the air's sensible heat, so the air cools and gains moisture along a near-constant wet-bulb (and enthalpy) line. Dry-bulb and W both change; RH rises.

Further reading: Singh and Heldman, Introduction to Food Engineering

2 · Psychrometry, humidification and dehumidification · medium

Air at 30 °C has a water vapour partial pressure of 2.0 kPa; the saturation vapour pressure at 30 °C is 4.246 kPa. Its relative humidity is closest to

  1. 212 %
  2. 47 %
  3. 1.3 %
  4. 2.0 %
Answer and working

B. 47 %

RH = pv/ps = 2.0/4.246 = 47 %. 212 % inverts the ratio and exceeds 100 %; 1.3 % is the humidity ratio expressed as a percentage; 2.0 % confuses kPa with per cent.

Further reading: Singh and Heldman, Introduction to Food Engineering

3 · Evaporation: boiling-point elevation and heat transfer · easy

10,000 kg/h of juice at 12 % solids is concentrated to 48 % solids. The water evaporated is

  1. 2,500 kg/h
  2. 7,500 kg/h
  3. 3,600 kg/h
  4. 9,750 kg/h
Answer and working

B. 7,500 kg/h

V = F(1 − xF/xP) = 10,000 × (1 − 12/48) = 7,500 kg/h. 2,500 kg/h is the concentrate; 3,600 kg/h multiplies the feed by the difference in percentages (10,000 × 0.36); 9,750 kg/h treats 12/48 as 2.5 %.

Further reading: Singh and Heldman, Introduction to Food Engineering

4 · Single- and multiple-effect evaporators; steam economy · medium

Backward feed in a multiple-effect evaporator is preferred when

  1. the product is heat-sensitive and must never meet the hottest effect
  2. no pumps are allowed between effects
  3. the concentrate is viscous and the feed is cold
  4. the feed is already above the first effect's boiling point
Answer and working

C. the concentrate is viscous and the feed is cold

Backward feed puts the most viscous liquid where temperature is highest and viscosity lowest, improving heat transfer, and suits cold feeds; it needs inter-effect pumps.

Further reading: Geankoplis, Transport Processes and Separation Process Principles

5 · Falling-film, forced-circulation and plate evaporators · easy

The evaporator type most widely used for concentrating milk and fruit juices is the

  1. open steam-jacketed pan
  2. falling-film evaporator
  3. short-tube natural-circulation evaporator
  4. agitated thin-film evaporator
Answer and working

B. falling-film evaporator

Falling-film units give short residence times at low ΔT and suit multiple effects and MVR. Open pans and short-tube units give long residence times; agitated thin-film units are for very viscous products.

Further reading: Fellows, Food Processing Technology

6 · Falling-film, forced-circulation and plate evaporators · medium

A rising-film (climbing-film) evaporator differs from a falling-film evaporator in that

  1. expanding vapour drives the film up the tubes, so a larger ΔT is needed
  2. the liquid flows down the tubes under gravity, so it works with very small differences
  3. the liquid is pumped at high velocity with boiling suppressed inside the tubes
  4. the liquid is spread by rotating blades on a heated cylinder wall
Answer and working

A. expanding vapour drives the film up the tubes, so a larger ΔT is needed

Climbing-film flow depends on vapour generation; falling-film flow uses gravity. The others describe forced-circulation and agitated thin-film evaporators.

Further reading: Geankoplis, Transport Processes and Separation Process Principles

7 · Spray drying: atomisation, powder properties and agglomeration · medium

Agglomeration (instantising) of a spray-dried powder improves

  1. oxidative stability, by removing all fat from the particle surfaces
  2. bulk density, by producing the finest possible single particles
  3. wettability and dispersibility, so the powder reconstitutes without lumps
  4. microbial safety, by sterilising the powder during rewetting
Answer and working

C. wettability and dispersibility, so the powder reconstitutes without lumps

Larger porous agglomerates wet and sink quickly. Agglomerates have lower bulk density, not higher, and rewetting does not sterilise.

Further reading: Fellows, Food Processing Technology

8 · Osmotic dehydration and intermediate-moisture foods · easy

Intermediate-moisture foods typically have a water activity of about

  1. 0.1 to 0.3
  2. 0.95 to 1.0
  3. 0.6 to 0.9
  4. 0.3 to 0.5
Answer and working

C. 0.6 to 0.9

IMFs are soft but shelf-stable, commonly aw 0.6–0.9 with 15–50 % moisture. Below 0.6 foods are dry; above 0.9 most bacteria grow.

Further reading: Fellows, Food Processing Technology

9 · Freeze concentration and membrane concentration · medium

The heat that must be removed to freeze 1 kg of water (latent heat of fusion) is about

  1. 2,260 kJ
  2. 2,840 kJ
  3. 334 kJ
  4. 4.18 kJ
Answer and working

C. 334 kJ

Fusion takes about 334 kJ/kg, much less than vaporisation (2,260 kJ/kg) or sublimation (2,840 kJ/kg); 4.18 kJ/kg K is the specific heat of water.

Further reading: Singh and Heldman, Introduction to Food Engineering

10 · Quality changes in dried foods and rehydration · hard

The selective diffusion theory explains aroma retention in spray-dried products by stating that

  1. a dried surface passes water far more readily than aroma molecules
  2. aroma molecules evaporate faster than water from the droplet throughout drying
  3. aromas are destroyed by heat and replaced by Maillard flavours
  4. aromas bind to the chamber walls and return to the powder later
Answer and working

A. a dried surface passes water far more readily than aroma molecules

As the droplet surface concentrates, diffusivity of larger aroma molecules falls far more than that of water, trapping aroma inside.

Further reading: Mujumdar, Handbook of Industrial Drying

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Read the subject

Evaporation, Dehydration & Concentration of FoodsThe full study manual, free GATEFormat, sections and how it has changed

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Evaporation, Dehydration & Concentration of Foods for other exams

GATE · IndiaICAR AICE-JRF/SRF · IndiaICAR AIEEA-PG / PGS · India

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