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GATE Fluid Flow, Thermodynamics & Heat Transfer in Dairy Plants: practice questions

GATE — Agricultural Engineering (AG), for dairy engineering aspirants · India · IITs and IISc on rotation

Original practice questions written to the published syllabus · not past papers
10worked here, free
30written to this exam in this subject
10syllabus units

What this subject covers

Fluid properties, pumping, thermodynamics and heat transfer worked as dairy plant problems.

In the exams: ICAR AICE subject 38 Units 1 and 4; ICAR AIEEA-PG group 17 Unit III (fluid mechanics, pumps, heat transfer, thermodynamics, dimensional analysis); GATE XL-U Section 4; GATE AG dairy and food engineering

Where the 30 questions fall

How our questions for GATE spread across the units of Fluid Flow, Thermodynamics & Heat Transfer in Dairy Plants. Difficulty: 6 easy, 21 medium, 3 hard.

Mass and energy balances in dairy processes5
Fluid properties and Bernoulli's equation4
Pipe flow, Reynolds number and friction losses4
Heat exchangers: LMTD and effectiveness-NTU4
Laws of thermodynamics; steam tables3
Conduction, convection and radiation3
Sanitary centrifugal and positive displacement pumps; pump selection2
Flow of non-Newtonian dairy fluids2
Fins and insulation2
Dimensionless numbers and dimensional analysis1

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 · Fluid properties and Bernoulli's equation · medium

Milk flows at 10 m³/h through a pipe of 51 mm internal diameter. What is its mean velocity?

  1. 5.44 m/s
  2. 0.34 m/s
  3. 4895 m/s
  4. 1.36 m/s
Answer and working

D. 1.36 m/s

A = π(0.051)²/4 = 2.04 × 10⁻³ m²; v = (10/3600)/A = 1.36 m/s. Forgetting the /4 in the area gives 0.34.

Further reading: Singh and Heldman, Introduction to Food Engineering

2 · Pipe flow, Reynolds number and friction losses · medium

Six bends each with K = 0.9 are in a line carrying milk at 1.5 m/s. What is the total minor loss?

  1. 0.10 m
  2. 0.62 m
  3. 0.41 m
  4. 12.15 m
Answer and working

B. 0.62 m

h_m = ΣK v²/2g = 6 × 0.9 × 0.1147 = 0.62 m.

Further reading: Singh and Heldman, Introduction to Food Engineering

3 · Sanitary centrifugal and positive displacement pumps; pump selection · medium

A centrifugal pump delivers 20 m³/h of milk against 25 m of head at 60% efficiency. What shaft power is needed?

  1. 2.34 kW
  2. 1.40 kW
  3. 0.84 kW
  4. 8420 kW
Answer and working

A. 2.34 kW

P = ρgQH/η = 1,030 × 9.81 × 0.00556 × 25/0.6 = 2,339 W = 2.34 kW. 1.40 kW is the hydraulic power.

Further reading: Singh and Heldman, Introduction to Food Engineering

4 · Flow of non-Newtonian dairy fluids · medium

A yoghurt follows τ = Kγ̇ⁿ with K = 10 Pa·sⁿ and n = 0.3. What is its apparent viscosity at 10 s⁻¹?

  1. 0.40 Pa·s
  2. 20.0 Pa·s
  3. 10.00 Pa·s
  4. 2.00 Pa·s
Answer and working

D. 2.00 Pa·s

μ_app = Kγ̇^(n−1) = 10 × 10^(−0.7) = 2.00 Pa·s; at 100 s⁻¹ it falls to 0.40 Pa·s.

Further reading: Steffe, Rheological Methods in Food Process Engineering

5 · Laws of thermodynamics; steam tables · medium

How much heat is needed to warm 5,000 kg/h of milk (c_p = 3.9 kJ/kg K) from 60 °C to 90 °C?

  1. 585 kW
  2. 174.2 kW
  3. 81.2 kW
  4. 162.5 kW
Answer and working

D. 162.5 kW

Q = ṁc_pΔT = 5,000 × 3.9 × 30 = 585,000 kJ/h = 162.5 kW. Using water's c_p gives 174.2 kW.

Further reading: Singh and Heldman, Introduction to Food Engineering

6 · Conduction, convection and radiation · medium

How much heat is conducted through 1 m² of stainless steel 0.6 mm thick (k = 16 W/m K) with 1 K across it?

  1. 0.0096 W
  2. 26.7 W
  3. 16 W
  4. 26,667 W
Answer and working

D. 26,667 W

Q = kAΔT/L = 16 × 1 × 1/0.0006 = 26,667 W. Using L in mm gives 26.7.

Further reading: Incropera et al., Fundamentals of Heat and Mass Transfer

7 · Heat exchangers: LMTD and effectiveness-NTU · medium

In a counter-current exchanger, hot water enters at 90 °C and leaves at 80 °C; milk enters at 60 °C and leaves at 75 °C. The LMTD is:

  1. 17.5 K
  2. 15.0 K
  3. 17.4 K
  4. 20.0 K
Answer and working

C. 17.4 K

ΔT₁ = 90 − 75 = 15 K, ΔT₂ = 80 − 60 = 20 K; LMTD = 5/ln(20/15) = 17.4 K, slightly below the arithmetic mean of 17.5 K.

Further reading: Singh and Heldman, Introduction to Food Engineering

8 · Heat exchangers: LMTD and effectiveness-NTU · easy

Raw milk enters a pasteuriser at 4 °C and leaves the regenerator at 66 °C; pasteurisation is at 72 °C. The regeneration efficiency is:

  1. 91%
  2. 92%
  3. 8%
  4. 86%
Answer and working

A. 91%

η_R = (66 − 4)/(72 − 4) = 62/68 = 91%. Dividing by 72 forgets the inlet temperature.

Further reading: Tetra Pak Dairy Processing Handbook

9 · Heat exchangers: LMTD and effectiveness-NTU · medium

A plate section has U = 3,000 W/m² K and A = 20 m² with an LMTD of 17.4 K. Its duty is about:

  1. 1050 kW
  2. 60 kW
  3. 1042818 kW
  4. 1043 kW
Answer and working

D. 1043 kW

Q = UA·LMTD = 3,000 × 20 × 17.4 = 1043 kW.

Further reading: Singh and Heldman, Introduction to Food Engineering

10 · Mass and energy balances in dairy processes · easy

10,000 kg/h of skim milk at 9% total solids is evaporated to 45% TS. How much water is removed?

  1. 2,000 kg/h
  2. 3,600 kg/h
  3. 8,000 kg/h
  4. 4,500 kg/h
Answer and working

C. 8,000 kg/h

Solids 900 kg/h; concentrate = 900/0.45 = 2,000 kg/h; water = 10,000 − 2,000 = 8,000 kg/h.

Further reading: Singh and Heldman, Introduction to Food Engineering

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Fluid Flow, Thermodynamics & Heat Transfer in Dairy PlantsThe full study manual, free GATEFormat, sections and how it has changed

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Instrumentation, Process Control & Automation

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