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BEE 2009 Question Paper with Answers — Paper-3

Energy Efficiency in Electrical Utilities
Available here with full solutions — 63 questions recovered from the 2009 exam:
Objective (1 mark)45 of 50
Short (5 marks)10 of 8
Long (10 marks)8 of 6
This is not the complete paper. The questions below are the ones we could recover and verify; the rest of that year’s paper is not reproduced here. Every answer shown is checked against the 2014 BEE guidebook and carries its book section reference and an explanation.

Full paper pattern: Section-I 50×1 = 50 marks · Section-II 8×5 = 40 · Section-III 6×10 = 60 · Total 150, pass mark 75, 3 hours.
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Other years

Objective questions (1 mark) — 45

📖 §4.3 & Table 4.3 Refrigerant / absorbent

1. Which of the following can be used as a refrigerant in both vapour compression and vapour absorption systems?

  1. ammonia
  2. R-11
  3. R-12
  4. lithium Bromide
Answer: A) ammonia
Confirmed vs Book-3 §4.3 - Ammonia (R-717) is used as the refrigerant in vapour compression systems and also as the refrigerant in ammonia-water vapour absorption systems. (In Li-Br systems, water is the refrigerant and lithium bromide is the absorbent.)
📖 §6.2 System characteristics — static & friction head

2. The friction loss in a pipe carrying a fluid is inversely proportional to the

  1. fluid flow
  2. square of the pipe diameter
  3. fluid velocity
  4. fifth power of pipe diameter
Answer: D) fifth power of pipe diameter
Confirmed vs Book-3 §6.2 — Friction head loss ∝ Q²/D⁵ for a given flow: halving the diameter multiplies loss ~32×. That is why the book says further friction reduction 'will require larger diameter pipe'. Friction loss is directly (not inversely) proportional to flow² and velocity², so a–c are wrong; 'square of diameter' badly understates the effect.
Chapter: Pumps
📖 §1.5 Transformers — losses & efficiency

3. Where transformer loading is known, the actual transformer loss at a given load can be computed as:

  1. No Load Loss + (Actual kVA/rated kVA) x Load Loss
  2. No Load Loss + (Actual kVA/rated kVA)² x Load Loss
  3. No Load Loss + (Actual kVA/rated kVA) x Load Loss²
  4. [No Load Loss + {(Actual kVA/rated kVA) x Load Loss}]²
Answer: B) No Load Loss + (Actual kVA/rated kVA)² x Load Loss
Confirmed vs Book-3 §1.5 — 'the actual transformer loss at given load = No load loss + (load kVA/Rated kVA)² × (Full load loss)', because copper loss varies with the square of the load current. Option (a) scales the copper loss linearly, which would badly over-estimate the loss at part load.
📖 Book-3 §3.5 Efficacy of Inter and After Coolers (Table 3.7)

4. The inlet air temperature to a two stage reciprocating air compressor is 35 °C. At which of the following 2nd stage inlet temperatures will the compressor consume least power?

  1. 75 °C
  2. 65 °C
  3. 60 °C
  4. 50 °C
Answer: D) 50 °C
Confirmed vs Book-3 §3.5 Efficacy of Inter and After Coolers (Table 3.7) — Table 3.7 shows that the nearer the second-stage inlet temperature is to the first-stage inlet ('perfect cooling'), the lower the specific power: a 5.5°C rise at the second-stage inlet costs about 2% more specific energy. With a 35°C first-stage inlet, 50°C is the closest of the four, so it gives the least power consumption; 75°C would be the worst.
📖 §1.1 Transmission & Distribution Lines — voltage vs. line loss (P=I²R)

5. In the city electrical distribution scheme, a proposal is being prepared to upgrade 33 kV network to 66 kV. The distribution loss, corresponding to the same quantum of load in the proposed upgraded system will be

  1. less by 25%
  2. less by 33%
  3. less by 75%
  4. none of the above
Answer: C) less by 75%
Confirmed vs Book-3 §1.1 — line loss varies as the inverse square of the voltage: (33/66)² = 1/4, so the loss falls to 25% of its old value, i.e. it is LESS by 75%. Option (a) 'less by 25%' quotes the remaining loss instead of the reduction — read the wording carefully.
📖 §2.7 Power Factor Correction — Table 2.5 Capacitor Ratings

6. Rating of power factor correction capacitors at induction motor terminals should be

  1. 100% of no load magnetizing kVAr of induction motor
  2. 90% of no load magnetizing kVAr of induction motor
  3. 120% of no load magnetizing kVAr of induction motor
  4. none of the above
Answer: B) 90% of no load magnetizing kVAr of induction motor
Confirmed vs Book-3 §2.7 Power Factor Correction — Table 2.5 Capacitor Ratings — Same rule: the capacitor is selected not to exceed 90 % of the motor's no-load (magnetizing) kVAr, which can only be established by a no-load test. (c) 120 % would leave the machine critically or over-corrected, risking self-excitation over-voltage on supply interruption.
📖 §1.4 Power Factor Improvement and Benefits

7. Select the correct statement:

  1. the advantage of PF improvement by capacitor addition in an electric network is that active power component of the network is reduced
  2. the power factor indicated in the monthly electricity bill is the lowest power factor recorded at any time during the billing month
  3. PF capacitors operating at lower voltage than their rated values have higher operating kVArs than their rated values
  4. the power factor of an induction motor decreases with decrease in percentage motor loading
Answer: D) the power factor of an induction motor decreases with decrease in percentage motor loading
Confirmed vs Book-3 §1.4 — an induction motor's magnetising (reactive) current is nearly constant while its kW falls with load, so kW/kVA — the power factor — falls as loading falls; this is why lightly loaded motors are a major cause of poor plant PF. Option (a) is wrong (capacitors do not reduce kW), (b) is wrong (the bill shows the AVERAGE PF, kWh/kVAh) and (c) is wrong (below rated voltage a capacitor gives LESS kVAr, since kVAr ∝ V²).
📖 §1.1 Cascade Efficiency

8. If the efficiencies of a power plant, transmission and distribution systems are 30%, 95% & 85% respectively, the cascade efficiency of power generation, and transmission system is given by

  1. 24.23%
  2. 28.5%
  3. 80.75%
  4. 95%
Answer: B) 28.5%
Confirmed vs Book-3 §1.1 Cascade Efficiency — the question asks only for generation AND transmission: 0.30 × 0.95 = 0.285 = 28.5%. Option (a) 24.23% is the full cascade INCLUDING the 85% distribution stage (0.30 × 0.95 × 0.85) — that stage was not asked for.
📖 §2.3 Motor Characteristics

9. What is the % slip of a 4 pole induction motor if the shaft speed at 49.5 Hz supply frequency is 1460 rpm?

  1. 1.68
  2. 2.66
  3. 1.71
  4. none of the above
Answer: A) 1.68
Corrected (was c) — Book-3 §2.3 Motor Characteristics: the slip formula uses the SYNCHRONOUS speed in the denominator. Ns = 120 × 49.5 / 4 = 1485 rpm, so slip = (1485 − 1460)/1485 × 100 = 1.68 % — option (a). The recorded 1.71 % comes from dividing by the rotor speed 1460 instead of by Ns; (b) 2.66 % comes from wrongly assuming Ns = 1500 rpm at 50 Hz.
📖 §2.2 Motor Types

10. During induction motor operation, magnetic field is established in

  1. stator winding only
  2. rotor winding only
  3. stator and rotor windings
  4. at carbon brushes
Answer: C) stator and rotor windings
Confirmed vs Book-3 §2.2 Motor Types — The stator carries the rotating flux and the induced rotor current creates its own alternating field, so a magnetic field exists in both stator and rotor windings; their interaction produces torque. (d) 'at carbon brushes' applies to a slip-ring or DC machine and has nothing to do with field production.
📖 §2.7 Motor Loading — Measuring Load

11. An induction motor rated for 7.5 kW and 90 % efficiency at full load, was drawing 5 kW. The percentage loading on the motor is

  1. 60 %
  2. 66.66%
  3. 74%
  4. none of the above
Answer: A) 60 %
Confirmed vs Book-3 §2.7 Motor Loading — Measuring Load — % loading = measured input / (rated kW ÷ rated efficiency) = 5 / (7.5/0.90) = 5 / 8.333 = 60 %. (b) 66.66 % is the trap of dividing 5 kW by the 7.5 kW OUTPUT rating, forgetting to convert the rating to its equivalent input.
📖 §1.2 Electricity Billing — trivector meter & Maximum Demand

12. If the apparent power drawn over a recording cycle of 30 minutes is 3000 kVA for 10 minutes, 2400 kVA for 15 minutes and 2900 kVA for 5 minutes, the MD recorder will compute MD as

  1. 3000 kVA
  2. 2400 kVA
  3. 2683 kVA
  4. none of the above
Answer: C) 2683 kVA
Confirmed vs Book-3 §1.2 — MD = time-integrated demand over the cycle = [(3000×10) + (2400×15) + (2900×5)]/30 = 80,500/30 = 2683 kVA. Option (a) 3000 kVA is the highest instantaneous block; the book stresses the meter registers the AVERAGE over the whole 30-minute recording cycle.
📖 Book-3 §3.5 Minimum Pressure Drop in Air Lines (Table 3.11)

13. The pressure drop in mains header at the farthest point of an industrial compressed air network shall not exceed

  1. 2 bar
  2. 0.3 bar
  3. 0.5 bar
  4. 1.0 bar
Answer: B) 0.3 bar
Confirmed vs Book-3 §3.5 Minimum Pressure Drop in Air Lines (Table 3.11) — Book-3: 'Typical acceptable pressure drop in industrial practice is 0.3 bar in mains header at the farthest point and 0.5 bar in distribution system.' The 0.5 bar figure offered in (c) is the distribution allowance, not the mains-header limit asked for.
📖 Book-3 §3.5 Pressure Settings / Reducing Delivery Pressure (Table 3.9)

14. At which of the following discharge pressures, the reciprocating air compressor will consume maximum power

  1. 3 bar
  2. 3.5 kg/cm2
  3. 150 psi
  4. 6 kg/cm2
Answer: C) 150 psi
Confirmed vs Book-3 §3.5 Pressure Settings / Reducing Delivery Pressure (Table 3.9) — Convert to common units: 3 bar ≈ 3.06 kg/cm², 3.5 kg/cm² ≈ 3.43 bar, 150 psi ≈ 10.34 bar (10.5 kg/cm²), 6 kg/cm² ≈ 5.88 bar. The highest by far is 150 psi. Since 'for the same capacity, a compressor consumes more power at higher pressures', 150 psi draws the maximum power; the trap is comparing the bare numbers across mixed units.
📖 Book-3 §3.5 Air Receivers (IS 7938-1976 sizing)

15. Which of the following is not true of air receivers?

  1. smoothens pulsating air output
  2. stores large volumes of air
  3. a source for draining moisture
  4. increases the pressure of air
Answer: D) increases the pressure of air
Confirmed vs Book-3 §3.5 Air Receivers (IS 7938-1976 sizing) — Air receivers smooth pulsating output, store large volumes for sudden demand and provide a point for draining precipitated moisture — (a), (b) and (c) are all true of them. A receiver holds air at the pressure the compressor delivers and cannot itself increase pressure, so (d) is the statement that is not true.
📖 §4.7 Ton of Refrigeration (TR)

16. A 1.5 ton air conditioner installed in a room and working continuously for two hours will remove heat of

  1. 3024 kCals
  2. 6048 kCals
  3. 9072 kCals
  4. none of the above
Answer: C) 9072 kCals
Confirmed vs Book-3 §4.7 - 1 TR = 3024 kCal/h; 1.5 TR × 2 h = 1.5 × 3024 × 2 = 9072 kCal. Option (a) is for 1 TR in one hour and (b) for 1.5 TR in one hour; multiply 3024 kcal/h by 1.5 TR and by 2 hours to get 9072 kcal.
📖 §4.7 TR formula (coolant side)

17. Chilled water enters evaporator at 12°C and leaves at 6°C. The flow rate of chilled water was measured as 300 m3/hr. The tons of refrigeration capacity is

  1. 0.595
  2. 595.24
  3. 35.7
  4. none of the above
Answer: B) 595.24
Confirmed vs Book-3 §4.7 - Heat = 300×1000×1×(12−6) = 1,800,000 kCal/h; TR = 1,800,000/3024 = 595.24 TR. Option (c) 35.7 divides by 3024 twice and (a) 0.595 misplaces the decimal; TR = 300,000 x 6/3024 = 595.24.
📖 §4.5 Centrifugal Compressors

18. Centrifugal compressors are most efficient when they are operating at_____.

  1. 50% load
  2. full load
  3. 75% load
  4. all load conditions
Answer: B) full load
Confirmed vs Book-3 §4.5 - Centrifugal (dynamic) compressors are most efficient at or near their design/full-load point. Options (a) and (c) describe part loads, where inlet-guide-vane throttling makes efficiency fall away sharply below 50%; the book says centrifugals are the most efficient type when operating NEAR FULL LOAD.
📖 §4.3 VAR COP vs VCR COP

19. The Coefficient of Performance (COP) of Vapour Absorption Refrigeration System (VAR)

  1. is higher than that of Vapour Compression Refrigeration (VCR) System
  2. is lower than that of Vapour Compression Refrigeration (VCR) System
  3. is same as that of Vapour Compression Refrigeration (VCR) System
  4. is normally 4 to 4.5
Answer: B) is lower than that of Vapour Compression Refrigeration (VCR) System
Confirmed vs Book-3 §4.3 - VAR systems typically have COP well below 1, much lower than vapour compression systems (COP 3–5). Option (a) reverses the comparison and (d) quotes a VCR-range COP; LiBr-water absorption machines run at COP 0.65-0.70 against 3-5 for compression chillers, which is why VAR pays only with cheap waste heat.
📖 §5.2 Fan types (Tables 5.2/5.3)

20. Backward-inclined fans are known as _____ because change in static pressure does not overload the motor

  1. overloading
  2. non-overloading
  3. radial
  4. axial
Answer: B) non-overloading
Confirmed vs Book-3 §5.2 — 'Backward-inclined fans are known as "non-overloading" because changes in static pressure do not overload the motor' — their power peaks and then falls within the usable flow range. Forward-curved fans, whose power rises continuously with flow, are the overloading type.
📖 §5.3 System characteristics & fan curves

21. The fan characteristic curve is a plot of

  1. static pressure vs flow
  2. dynamic pressure vs flow
  3. total pressure vs flow
  4. suction pressure vs flow
Answer: A) static pressure vs flow
Confirmed vs Book-3 §5.3 — Among the manufacturer's curves 'the curve static pressure (SP) vs. flow is especially important'; its intersection with the system curve defines the operating point. Total/dynamic/suction pressure vs flow (b, c, d) are not the standard fan characteristic.
📖 §6.1 Hydraulic power, pump shaft power & motor input power (p.172)

22. The hydraulic power of a motor pump set is 8.5 kW. If the power drawn by the motor is 15.5 kW at a 89% efficiency, the pump efficiency is given by

  1. 54.8%
  2. 61.6%
  3. 48.8%
  4. none of the above
Answer: B) 61.6%
Confirmed vs Book-3 §6.1 — Pump shaft power = 15.5×0.89 = 13.795 kW; pump efficiency = 8.5/13.795 = 61.6%. 54.8% (8.5/15.5) ignores motor efficiency; 48.8% wrongly multiplies that by 0.89.
Chapter: Pumps
📖 §6.2 System characteristics — static & friction head

23. For the same flow through which of the following diameter pipes, the pump will work with maximum pressure

  1. 80 mm
  2. 100 mm
  3. 120 mm
  4. 140 mm
Answer: A) 80 mm
Confirmed vs Book-3 §6.2 — For a fixed flow the smallest pipe (80 mm) gives the highest velocity and friction loss (∝ 1/D⁵), so the pump must work against the maximum pressure. Larger pipes reduce friction head — the book's rationale for larger diameter pipe. (Option d corrected from OCR '1400 mm' to '140 mm'.)
Chapter: Pumps
📖 §7.2 Cooling Tower Performance (iii) Effectiveness

24. If inlet and outlet water temperatures of a cooling tower are 44°C and 38°C respectively and atmospheric DBT and WBT are 40°C and 35°C respectively, then the effectiveness of cooling tower is

  1. 54.5%
  2. 66.6%
  3. 75%
  4. none of the above
Answer: B) 66.6%
Corrected (was a) — Book-3 §7.2 (iii): Effectiveness = Range/(Range + Approach) × 100. Range = 44 − 38 = 6°C; Approach = 38 − 35 = 3°C (cold water − WBT, DBT is a distractor); Effectiveness = 6/(6 + 3) = 66.6% → (b). 54.5% (a) = 6/11 would only result if the WBT were 33°C (approach 5°C) – it does not follow from the figures printed here. ⚠ Answer changed a→b: with the printed data (WBT 35°C) the book formula gives 66.6%. The old key value 54.5% corresponds to a 33°C WBT variant of this question.
📖 §6.1 Hydraulic power, pump shaft power & motor input power (p.172)

25. The motor efficiency is 0.9 and the pump efficiency is 0.6. The input power to the motor driving the pump is 28 kW. The power transmitted to the water is

  1. 15.12 kW
  2. 28 kW
  3. 25.2 kW
  4. none of the above
Answer: A) 15.12 kW
Confirmed vs Book-3 §6.1 — Power to water (hydraulic) = motor input × η_motor × η_pump = 28×0.9×0.6 = 15.12 kW. 25.2 kW is only the motor shaft output (28×0.9); 28 kW is the electrical input.
Chapter: Pumps
📖 §6.5 Effects of impeller diameter change (Q∝D, H∝D², P∝D³; trim limited to ~75%)

26. A water pump is delivering 200 m3/hr at ambient conditions. The impeller diameter is trimmed by 10%. The water flow at the changed conditions is

  1. 220 m3/hr
  2. 180 m3/hr
  3. 162 m3/hr
  4. none of the above
Answer: B) 180 m3/hr
Confirmed vs Book-3 §6.5 — Q∝D: a 10% trim gives Q₂ = 0.9×200 = 180 m³/hr. 162 m³/hr (0.9²×200) wrongly uses the head relation; 220 would be an enlarged impeller.
Chapter: Pumps
📖 §4.8 Table 4.5 (condenser temperature)

27. At which of the following condenser temperatures, the power consumption of a vapour compression refrigeration system will be the least

  1. 26°C
  2. 28°C
  3. 29°C
  4. 25°C
Answer: D) 25°C
Confirmed vs Book-3 §4.8 - Lower condensing temperature reduces compressor lift and power; 25°C is the lowest, giving least power. Every other option is a higher condensing temperature, and Table 4.5 shows specific power consumption rising steadily with condenser temperature - lower condensing temperature means a smaller compression lift.
📖 §7.2 Factors Affecting Performance – Wet Bulb Temperature

28. Which of the following ambient conditions will not evaporate maximum amount of water in a cooling tower

  1. 41°C DBT and 38°C WBT
  2. 38°C DBT and 37°C WBT
  3. 36°C DBT and 30°C WBT
  4. 36°C DBT and 31°C WBT
Answer: B) 38°C DBT and 37°C WBT
Confirmed vs Book-3 §7.2 Wet Bulb Temperature — Evaporation is driven by the wet-bulb depression (DBT − WBT). Options (c) and (d) have 6 and 5°C depression and evaporate a lot; (b) 38/37°C has only 1°C – near-saturated air – so it is the condition that will NOT evaporate the maximum → (b).
📖 §7.2 Cooling Tower Performance (ii) Approach

29. If inlet and outlet water temperatures of a cooling tower are 39°C and 33°C respectively and atmospheric DBT and WBT are 35°C and 28°C respectively then the approach of cooling tower is

  1. 3°C
  2. 4°C
  3. 5°C
  4. 6°C
Answer: C) 5°C
Confirmed vs Book-3 §7.2 (ii) — Approach = outlet cold water temperature − ambient WBT = 33 − 28 = 5°C → (c). Using DBT (35 − 33 = 2°C) or range (39 − 33 = 6°C, option d) are the common traps.
📖 §7.2 Cooling Tower Performance (iv) Cooling capacity

30. If flow rate is 100 m3/hr and the range is 8°C for a cooling tower, then its heat load in kCal/hr will be

  1. 800
  2. 8,000
  3. 80,000
  4. 800,000
Answer: D) 800,000
Confirmed vs Book-3 §7.2 (iv) — Heat load = mass flow × Cp × Range = 100 m³/hr × 1000 kg/m³ × 1 kcal/kg°C × 8°C = 8,00,000 kcal/hr → (d). Forgetting the ×1000 (m³ → kg) gives 800 (a).
📖 §8.6(e) Reduction of lighting feeder voltage + Table 8.3

31. If voltage is increased from 230 V to 250 V for a fluorescent tube light, it will result in

  1. reduced power consumption
  2. increased power consumption
  3. decreased light levels
  4. no change in power consumption and light levels
Answer: B) increased power consumption
Confirmed vs Book-3 §8.6(e) Table 8.3 — For fluorescent lamps a 10 % higher voltage increases power input by 8.1 % (and light output by only 8 %); higher voltage also reduces lamp life. So 230 → 250 V raises power consumption; it does not reduce light level.
Chapter: Lighting
📖 §1.4 Automatic Power Factor Controllers

32. Automatic power factor controller using kVAr control, requires sensing of

  1. current
  2. voltage
  3. capacitance
  4. both a and b
Answer: D) both a and b
Confirmed vs Book-3 §1.4 — an APFC computes the reactive power/displacement power factor, which requires both the current and the voltage (and the angle between them) to be sensed before it can switch capacitor steps. Option (a) alone gives no angle information, so no kVAr or PF can be derived from current sensing by itself.
📖 §4.7 COP & kW/TR

33. The COP of a vapour compression system is 3.0. If the motor draws power of 11 kW at 90% motor efficiency, the cooling effect of vapour compression system will be

  1. 29.7 kW
  2. 37.8 kW
  3. 0.36 kW
  4. none of the above as cooling effect is always measured in TR
Answer: A) 29.7 kW
Confirmed vs Book-3 §4.7 - Shaft power = 11×0.9 = 9.9 kW; cooling effect = COP × power = 3.0 × 9.9 = 29.7 kW. Option (b) 37.8 kW ignores the 90% motor efficiency; shaft power = 11 x 0.9 = 9.9 kW, and cooling effect = COP x shaft power = 29.7 kW.
📖 §4.11 Heat Pumps and Their Applications

34. Which of the following can also act as a heat pump?

  1. centrifugal pump
  2. centrifugal compressor
  3. air conditioner
  4. none of the above
Answer: C) air conditioner
Confirmed vs Book-3 §4.11 - A reversible air conditioner can deliver heat (heat pump mode) as well as cooling. A centrifugal pump (a) moves liquid and a compressor alone (b) is only a component; §4.11 states a heat pump is the same as an air conditioner except that the rejected heat becomes the useful output.
📖 §4.5 Screw Compressors; §4.17 Case Study

35. A slide valve is used for capacity control in which of the following refrigeration compressors?

  1. reciprocating
  2. centrifugal
  3. screw
  4. scroll
Answer: C) screw
Confirmed vs Book-3 §4.5 - Screw compressors use a sliding slide valve to vary the effective rotor length and hence capacity. Reciprocating machines (a) unload cylinders, centrifugals (b) use inlet guide vanes and scrolls (d) have no capacity control of this kind; §4.5 and the §4.17 case study name the slide valve as the common screw-compressor control (10-100%).
📖 §2.9 Application of Variable Speed Drives — Concept & Principles of VFD

36. The largest potential for electricity savings with variable speed drives is generally for:

  1. variable torque applications
  2. constant torque loads
  3. constant power load
  4. combination of above
Answer: A) variable torque applications
Confirmed vs Book-3 §2.9 Application of Variable Speed Drives — Concept & Principles of VFD — The book states the largest potential for electricity savings with VSDs is generally in variable torque applications such as centrifugal pumps and fans, where power changes as the cube of speed — a 20 % speed cut gives almost 50 % input power reduction. (b) constant torque loads are also suitable for VSDs but their power falls only linearly with speed, so the savings are smaller.
📖 §1.3 Electrical Load Management and Maximum Demand Control

37. Maximum demand controller is used to

  1. switch off non-essential loads in a logical sequence
  2. switch off essential loads in a logical sequence
  3. controls the reactive power of the plant
  4. all the above.
Answer: A) switch off non-essential loads in a logical sequence
Confirmed vs Book-3 §1.3 Shedding of Non-Essential Loads — the MD controller provides 'Automatic load shedding in a predetermined sequence' and 'Automatic restoration of load' when the demand approaches a preset limit. Option (b) is wrong: only NON-essential loads are shed; option (c) describes an APFC, which handles reactive power.
📖 §2.9 Other Methods of Speed Control — Fluid Coupling / Eddy Current Drives

38. In a fluid coupling, connecting an induction motor and a fan

  1. motor speed can be changed by the fluid coupling
  2. fan speed can be changed by the fluid coupling
  3. both motor and fan speed can be changed by the fluid coupling
  4. none of the above is possible
Answer: B) fan speed can be changed by the fluid coupling
Confirmed vs Book-3 §2.9 Other Methods of Speed Control — Fluid Coupling / Eddy Current Drives — A fluid coupling varies the speed of the DRIVEN equipment without changing the speed of the motor — the impeller runs at motor speed and slip between impeller and runner sets the output speed. (a)/(c) are wrong precisely because the motor stays on a fixed-frequency supply and keeps its own speed.
📖 Not in Book-3 Ch5 text (belt drive slip; cf. §5.5 Pulley change)

39. In a "V" belt coupled fan drive, the measured speed at motor end 6" diameter pulley is 1480 rpm and that at fan end 10" diameter pulley is 820 RPM. What is the slippage loss in %?

  1. 7.66
  2. 8.29
  3. 6.67
  4. insufficient data, cannot be worked out
Answer: B) 8.29
Confirmed vs official key (topic not covered in Book-3 Ch5) — Theoretical fan speed = 1480 × 6/10 = 888 rpm; actual 820 rpm, so speed lost to slip = 68 rpm. The official key (b) 8.29% expresses this relative to the ACTUAL fan speed: 68/820 = 8.29%. Relative to the theoretical speed it would be 68/888 = 7.66% (option a) — follow the official key in the exam. The data is sufficient, so (d) is wrong.
📖 §8.6(f) Electronic ballasts

40. The electronic ballast in lighting application does not have one of the following characteristics

  1. lower operational losses than conventional ballasts
  2. tuned circuit to deliver power at 28-32 kHz
  3. requiring a starter
  4. low temperature rise
Answer: C) requiring a starter
Confirmed vs Book-3 §8.6(f) — Electronic ballasts: losses ~1 W vs 10–15 W (lower losses, low temperature rise), operate the lamp at high frequency (book 20–30 kHz), and 'the starter is eliminated' — so 'requiring a starter' is the characteristic it does not have.
Chapter: Lighting
📖 §7.2 Cooling Tower Performance (vii) Blow down

41. Increasing the cycles of concentration of circulating water in a cooling tower will

  1. increase blow down quantity
  2. decrease blow down quantity
  3. increase drift losses
  4. decrease fan power consumption
Answer: B) decrease blow down quantity
Confirmed vs Book-3 §7.2 (vii) — Blow Down = Evaporation/(COC − 1); a higher COC lowers the blowdown quantity → (b). Drift loss is set by the eliminators and air velocity, and fan power by air flow – neither depends on COC. ⚠ Option d repaired: garbled 'decrease bar create power consumption' → 'decrease fan power consumption'.
📖 §9.2 Sizing — kVA = √3·V·I; §9.4 specific fuel consumption

42. In a DG set, a 3-phase alternator is supplying on an average 100 A at 420 V and 0.9 pf to a load. If the specific fuel consumption of this DG set is 0.30 lit/kWh at that load, then how much fuel is consumed while delivering generated power for one hour?

  1. 11.34 litre
  2. 19.64 litre
  3. 21.82 litre
  4. 65.50 litre
Answer: B) 19.64 litre
Confirmed vs Book-3 §9.2/§9.4 — Power = √3 × 420 × 100 × 0.9 = 65,466 W = 65.47 kW; fuel = 65.47 × 0.30 = 19.64 litres per hour. (c) 21.82 L ignores the 0.9 PF; (d) 65.50 is the kW value mis-read as litres.
Chapter: DG Sets
📖 Book-3 §3.2 Positive Displacement — Reciprocating Compressors

43. The compressor capacity of a reciprocating compressor is directly proportional to __________.

  1. Speed
  2. Pressure
  3. Volume
  4. All
Answer: A) Speed
Confirmed vs Book-3 §3.2 Positive Displacement — Book-3 §3.2: 'the compressor capacity is directly proportional to the speed' — halving the RPM (e.g. by reducing the motor pulley) halves the delivered air, which is the basis of the pulley-change de-rating measure. Output stays nearly constant over a range of discharge pressures, so capacity is not proportional to pressure, and 'All' is therefore wrong.
📖 §2.4 Motor Efficiency

44. Select the incorrect statement:

  1. slip ring induction motors are normally less efficient than squirrel cage induction motors
  2. high speed squirrel cage induction motors are normally less efficient than low speed squirrel cage induction motors
  3. the capacitor requirement for PF improvement at induction motor terminal increases with decrease in rated speed of the induction motor
  4. induction motor efficiency increases with increase in its rated capacity
Answer: B) high speed squirrel cage induction motors are normally less efficient than low speed squirrel cage induction motors
Confirmed vs Book-3 §2.4 Motor Efficiency — The book states that 'higher-speed motors are normally more efficient than lower-speed motors', so statement (b) reverses the book and is the incorrect one. (a), (c) and (d) are all book-supported — squirrel cage beats slip-ring on efficiency, capacitor kVAr rises as speed falls (Table 2.5), and motor efficiency increases with rated capacity.
📖 §5.2 Fan types (axial vs centrifugal)

45. In which of the following fans air enters and leaves the fan with no change in direction ?

  1. Forward curved
  2. Backward curved
  3. Radial
  4. Propeller
Answer: D) Propeller
Forward-curved, backward-curved and radial are all CENTRIFUGAL impellers — air enters at the eye axially and is discharged radially, a 90° change of direction. Only the propeller fan (an axial machine) passes air straight through parallel to the shaft. Same idea as the tube-axial/vane-axial question, asked the other way round.

Short questions (5 marks) — 10

📖 Book-3 §3.6 Compressor Capacity Assessment (shop-floor pump-up method)

1. Calculate the free air delivery (FAD) capacity of a compressor in m3/hr for: receiver capacity 0.3 m3, initial pressure 0 kg/cm2(g), final pressure 7 kg/cm2(g), initial air temperature 35 degC, final air temperature 50 degC, additional holdup volume 0.05 m3, compressor pump-up time 4.1 minutes, atmospheric pressure 1.026 kg/cm2(a).

Model answer: Total system volume V = 0.3 + 0.05 = 0.35 m3. FAD = [(P2 - P1)/P0] x V / t, corrected for temperature. P2 - P1 = (7+1.026) - (0+1.026) = 7.0 kg/cm2; P0 = 1.026 kg/cm2(a). Volume of free air = (7.0/1.026) x 0.35 = 2.388 m3 in 4.1 min. FAD per minute = 2.388/4.1 = 0.5825 m3/min = 34.95 m3/hr. Applying the temperature correction (273+35)/(273+50) = 308/323 = 0.954, FAD ≈ 34.95 x 0.954 ≈ 33.3 m3/hr.
Confirmed vs Book-3 §3.6 Compressor Capacity Assessment — FAD = [(P2-P1)/atmospheric] x (receiver+holdup) / pump-up time, with temperature correction; gives about 33 m3/hr.
📖 §4.16 Energy Saving Opportunities

2. Discuss in brief any three methods by which energy can be saved in an air conditioning system.

Model answer: 1) Raise the chilled water / cold air set-point temperature (and reduce condenser water/refrigerant condensing temperature) to lower the temperature lift and improve COP. 2) Reduce the cooling load - improve building insulation, use solar films/shading, control fresh-air infiltration and ventilation, and switch off unnecessary loads. 3) Operate chillers at optimum loading and use efficient part-load control (VFDs on pumps/AHU fans, optimum sequencing of multiple chillers), keep heat-exchanger surfaces (condenser/cooling tower) clean, and maintain correct refrigerant charge. These reduce kW/TR and overall energy use.
Reduce temperature lift, cut the cooling load, and optimize chiller/auxiliary operation (clean surfaces, VFDs, sequencing) to lower kW/TR.
📖 §6.1 Hydraulic power, pump shaft power & motor input power (p.172); 1 kg/cm² ≈ 10 m water; suction lift (level below centreline) adds to head

3. A pump is delivering 50 m3/hr of water with a discharge pressure of 3.5 kg/cm2. The water is drawn from a sump where water level is 5 meter below the pump centerline. The power drawn by the motor is 9.5 kW at 90% motor efficiency. Find out the pump efficiency.

Model answer: Total head = discharge head + suction lift = (3.5 kg/cm2 x 10 m/(kg/cm2)) + 5 m = 35 + 5 = 40 m. Flow = 50 m3/hr = 50/3600 = 0.01389 m3/s. Hydraulic power = (rho x g x Q x H)/1000 = (1000 x 9.81 x 0.01389 x 40)/1000 = 5.45 kW. Pump shaft power = motor input x motor efficiency = 9.5 x 0.90 = 8.55 kW. Pump efficiency = hydraulic power / shaft power = 5.45 / 8.55 = 0.637 = about 64%.
Total head 40 m, hydraulic power about 5.45 kW, shaft power 8.55 kW, so pump efficiency is roughly 64%.
Chapter: Pumps
📖 §7.2 Cooling Tower Performance (iv) Cooling capacity (Book EOC S-1)

4. Estimate the cooling tower capacity (TR) with: water flow rate 120 m3/h, sp. heat 1 kcal/kg C, inlet water temperature 37 C, outlet water temperature 32 C, ambient WBT 29 C.

Model answer: Heat rejected = mass flow × sp. heat × Range. Water flow = 120 m³/h = 120,000 kg/h. Range = 37 − 32 = 5°C. Heat load = 120,000 × 1 × 5 = 6,00,000 kcal/h. 1 TR = 3024 kcal/h, so capacity = 6,00,000 / 3024 = 198.4 TR (≈ 200 TR). (Approach = 32 − 29 = 3°C; the WBT is not needed for the TR figure.)
Heat load = 120000 kg/h x 1 x 5 C = 6.0 lakh kcal/h; dividing by 3024 kcal/h per TR gives about 198 TR.
📖 §5.6 Fan static efficiency formula (Book EOC S-2)

5. A fan delivers 18,500 Nm³/hr at static pressure rise 45 mm WC. The 3-phase motor records 2.9 kW/phase; motor operating efficiency 88%. What is the fan static efficiency?

Model answer: Q = 18,500 Nm³/hr = 5.13888 m³/s; SP = 45 mmWC. Power input to motor = 2.9 x 3 = 8.7 kW. Power to fan shaft = 8.7 x 0.88 = 7.656 kW. Fan static efficiency = (5.13888 x 45)/(102 x 7.656) = 0.296 = 29.6%.
Book-3 §5.6: shaft kW = 3 × 2.9 × 0.88 = 7.656 kW; η_static = (5.139 × 45)/(102 × 7.656) = 29.6%.
📖 §1.4 Performance Assessment of Power Factor Capacitors

6. a) A 10 kVAr, 415 V rated power factor capacitor was found to be having terminal supply voltage of 440 V. Calculate the capacity of the power factor capacitor at the operating supply voltage. b) What would be the nearest kVAr compensation required for changing the power factor of a 500 kW load from 0.9 lead to unity power factor?

Model answer: a) Capacitor output varies as the square of the applied voltage (Book-3 Sec.1.4, Voltage effects): kVAr = 10 x (440/415)^2 = 10 x 1.124 = 11.24 kVAr. The bank delivers more than its rating, but running above rated voltage shortens capacitor life. b) At 0.9 LEADING the load is already over-compensated - the current leads the voltage - so NO further capacitive kVAr is required. To reach unity, capacitance must instead be REMOVED: excess kVAr = 500 x tan(cos^-1 0.9) = 500 x 0.4843 = 242 kVAr of the existing bank should be switched out.
a) Capacitor kVAr varies with square of voltage ratio. b) Load is already at leading PF, so additional capacitive compensation is not needed.
📖 §4.7 TR definition & air-side TR formula

7. Define one 'Ton of Refrigeration (TR)'. How do you calculate TR across the Air Handling Units?

Model answer: A ton of refrigeration is the quantity of heat to be removed to form one ton of ice in 24 hours when the initial water temperature is 0°C, equivalent to 50.4 kCal/min or 3024 kCal/h. Refrigeration load TR = Q × ρ × (h_in − h_out) / 3024, where Q is air flow in CMH, ρ is air density (kg/m³), h_in and h_out are enthalpies of inlet and outlet air (kCal/kg).
Definition of TR plus the AHU enthalpy-difference method for computing cooling load across the unit.
📖 §5.6 Fan static efficiency formula

8. A fan is delivering 20,000 Nm3/hr of air at static pressure difference of 70 mm WC. If the fan static efficiency is 55%, find out the shaft power of the fan.

Model answer: Q = 20,000/3600 = 5.56 m³/s. Fan static efficiency = (Q × Pst)/(102 × shaft power). 0.55 = (5.56 × 70)/(102 × P), giving shaft power P = 6.94 kW.
Rearrange Book-3 §5.6: shaft kW = (Q × SP)/(102 × η) = (5.56 × 70)/(102 × 0.55) = 389/56.1 = 6.94 kW.
📖 §2.7 Motor Loading — Measuring Load

9. A 15 kW, 415 V, 26 A, 4 pole, 50 Hz, 3 phase squirrel cage induction motor has full load efficiency and power factor of 90% and 0.89. An energy auditor measures: Supply voltage 408 V, Current 15 A, PF 0.81, Supply frequency 49.9 Hz, RPM 1488. Find at the operating conditions: 1) Power input in kW, 2) % motor loading, 3) % slip.

Model answer: 1) Power input = √3 × V × I × PF = 1.732 × 408 × 15 × 0.81 = 8,586 W = 8.59 kW. 2) Rated input = rated output / full-load efficiency = 15 / 0.90 = 16.67 kW; % motor loading = 8.59 / 16.67 × 100 = 51.5 %. (Using the nameplate √3 × 415 × 26 × 0.89 = 16.63 kW gives the same 51.6 %. The current ratio 15/26 = 58 % must NOT be used — the book forbids estimating loading from currents.) 3) Synchronous speed at 49.9 Hz = 120 × 49.9 / 4 = 1,497 rpm; % slip = (1,497 − 1,488)/1,497 × 100 = 0.60 %.
Power input from √3×V×I×PF; loading vs rated input (rated kW/efficiency); slip from synchronous speed at measured frequency.
📖 Book-3 §3.5 Avoiding Air Leaks — leak quantification (Tables 3.16 & 3.17)

10. A compressed air leakage test was conducted in an industry running 3 nos. of 500 cfm reciprocating compressors, maintained at loading-unloading settings of 6.6 and 7.0 kg/cm2g. Trial 1 (before): On load 30 secs, Unload 110 secs. Trial 2 (after attending leaks): On load 18 secs, Unload 145 secs. Average power was 71 kW during load and 16 kW during unload. Calculate the annual cost savings for 4000 hr/year operation at energy charge Rs. 6.00 per kWh.

Model answer: Leakage (trial 1) = (30×500)/(30+110) = 107 cfm. Leakage (trial 2) = (18×500)/(18+145) = 55 cfm. Specific power consumption = 71/(500×60) = 0.0023666 kW/ft³. Reduction in leakage = 107−55 = 52 cfm = 3120 cfh. Energy saving per hour = 3120 × 0.0023666 = 7.3838 kWh. Annual cost saving = 7.3838 × 4000 × 6 = Rs. 1,77,211 per annum.
Confirmed vs Book-3 §3.5 Avoiding Air Leaks — leak quantification — Leakage quantity from load fraction × FAD; specific power per ft³; multiply leakage reduction by specific power, operating hours and tariff.

Long questions (10 marks) — 8

📖 Book-3 §3.6 Compressor Capacity Assessment (shop-floor pump-up method); Book-3 §3.5 Avoiding Air Leaks — leak quantification (Tables 3.16 & 3.17)

1. A free air delivery test was carried out before conducting a leakage test on a reciprocating air compressor in an engineering industry, with the following observations: Receiver capacity 8.0 m3; Initial pressure 0.1 kg/cm2(g); Final pressure 7.0 kg/cm2(g); Additional hold-up volume 0.3 m3; Atmospheric pressure 1.026 kg/cm2 abs; Compressor pump-up time 3.5 minutes. During the subsequent leakage test at lunch time, with no pneumatic equipment or control valves in operation: (a) compressor on-load time 24 seconds at an unloading pressure of 7 kg/cm2(g); (b) average power drawn during loading 92 kW; (c) compressor unload time 79 seconds and loading pressure 6.6 kg/cm2(g). Find: (i) compressor output in m3/hr (neglect temperature correction); (ii) specific power consumption in kW/(m3/hr); (iii) % air leakage in the system; (iv) leakage quantity in m3/hr; (v) power lost due to leakage.

Model answer: Total system volume V = 8.0 + 0.3 = 8.3 m3. (i) Compressor output Q = [(P2 - P1)/P0] x V/t = [(7.0 - 0.1)/1.026] x (8.3/3.5) = 6.725 x 2.371 = 15.94 m3/min = 956.6 m3/hr (temperature correction neglected as stated). (ii) Specific power consumption = 92 kW / 956.6 m3/hr = 0.0962 kW per m3/hr. (iii) % air leakage = T/(T+t) x 100 = 24/(24+79) x 100 = 23.30%. (iv) Leakage quantity = 0.2330 x 956.6 = 222.9 m3/hr (= 3.71 m3/min). (v) Power lost due to leakage = leakage quantity x specific power consumption = 222.9 x 0.0962 = 21.4 kW.
Confirmed vs Book-3 §3.6 Compressor Capacity Assessment — L-2 as printed: FAD = [(P2-P1)/Patm] x (receiver + hold-up)/pump-up time, then % leakage = load/(load+unload), leakage quantity = % x FAD and power lost = leakage quantity x specific power. The stem was restored from the book (pump-up time 3.5 min and the full leakage data were missing) and the item re-typed as Long, per its own source line.
📖 §7.3 Efficient System Operation – IV Performance Assessment of Cooling Towers (Book EOC L-1 – identical to book trial)

2. A cooling tower cools 1565 m3/hr of water from 44 C to 37.6 C at 29.3 C wet bulb temperature. The fan air flow rate is 989544 m3/hr (air density 1.08 kg/m3) and it operates at 2.7 cycles of concentration. Find: a) Range, b) Approach, c) % CT Effectiveness, d) L/G ratio in kg/kg, e) Cooling duty in TR, f) Evaporation losses in m3/hr, g) Blowdown in m3/hr, h) Make-up water in m3/hr.

Model answer: a) Range = 44 − 37.6 = 6.4°C. b) Approach = 37.6 − 29.3 = 8.3°C. c) Effectiveness = Range/(Range + Approach) × 100 = 6.4/(6.4 + 8.3) × 100 = 43.53%. d) Water mass L = 1565 × 1000 = 15,65,000 kg/hr; air mass G = 989544 × 1.08 = 10,68,708 kg/hr; L/G = 15,65,000/10,68,708 = 1.46 kg/kg. e) Cooling duty = 1565 × 1000 × 1 × 6.4 = 1,00,16,000 kcal/hr = 10016 × 10³ kcal/hr; in TR = 1,00,16,000/3024 ≈ 3312 TR. f) Evaporation loss = 0.00085 × 1.8 × 1565 × 6.4 = 15.32 m³/hr (≈ 0.97% of circulation). g) Blow down = Evaporation/(COC − 1) = 15.32/(2.7 − 1) = 9.01 m³/hr. h) Make-up water = Evaporation + Blow down = 15.32 + 9.01 = 24.33 m³/hr (book's printed '2433' is a typo for 24.33).
Book trial values (§7.3 IV): Range 6.4°C, Approach 8.3°C, Effectiveness 43.53%, L/G 1.46 kg/kg, Duty 10016 × 10³ kcal/hr ≈ 3312 TR, Evaporation 15.32 m³/hr, Blowdown 9.01 m³/hr, Make-up 24.33 m³/hr.
📖 §1.1 Power Generation Plant — Heat Rate & generation efficiency — multi-chapter fill-in-the-blanks

3. Fill in the blanks: a) Heat Rate of a thermal power plant is expressed in ____. b) With increase in design speed of induction motors, the required capacitive kVAr for reactive power compensation for the same capacity range will ____. c) An air dryer in a compressed air system reduces ____ point of air. d) A Pitot tube measures the difference between ____ and ____ pressures of the fluid. e) The friction loss in a pipe carrying a fluid is proportional to the ____ power of pipe diameter.

Model answer: a) kCal/kWh b) decrease c) dew (dew point) d) total and static e) fifth
Standard BEE definitions: heat rate in kCal/kWh; higher-speed motors need less magnetizing kVAr; air dryer lowers dew point; Pitot tube reads total minus static pressure; pipe friction loss ∝ 1/d⁵ (fifth power of diameter).
📖 §8.3(1) Incandescent lamp; §8.2 Control gear (discharge lamps); §8.6 Energy saving opportunities

4. a) Briefly explain the difference between a 'filament lamp' and a 'gas discharge lamp'. b) State any 3 best practices in a lighting system for energy savings.

Model answer: a) Filament lamps (e.g. incandescent) produce light by a filament heated to incandescence by the flow of electric current through it. A gas discharge lamp produces light not by heating a filament but by the excitation of gas contained in a tubular or elliptical outer bulb. b) Any three of: install energy efficient fluorescent lamps in place of conventional ones; CFLs in place of incandescent lamps; metal halide lamps in place of mercury/sodium vapour lamps; HPSV lamps where colour rendering is not critical; LED indicator lamps in place of filament lamps; optimum daylighting; grouping of lighting for control flexibility; microprocessor based controllers; exclusive lighting transformer; servo stabilizer on lighting feeder; high-frequency electronic ballasts in place of conventional ballasts.
Book-3 §8.3: filament lamp = wire heated to incandescence by current; discharge lamp = current through low-pressure mercury vapour/gas between electrodes (needs ballast/ignitor, §8.2). Best practices from §8.6/§8.7: efficient lamps per Table 8.1, electronic ballasts, feeder-voltage optimisation, daylighting, controls.
Chapter: Lighting
📖 §1.5 Transformers — losses & efficiency

5. a) A small scale industry has a constant load of 380 kVA. It has installed two transformers of 500 kVA each. The no load loss and full load copper loss of each 500 kVA transformer is 750 W and 5410 W respectively. From the energy efficiency point of view should the industry operate a single transformer or two transformers equally sharing the load? b) A no load test on a three phase delta connected induction motor gave: No load power = 890 W, Stator resistance per phase at 30°C = 0.233 Ohms, No load current = 14.5 A. Calculate the fixed losses for the motor.

Model answer: a) Single 500 kVA at 380 kVA load: loss = 750 + (380/500)² × 5410 = 750 + 3124.8 = 3874.8 W. Two transformers each at 190 kVA: loss = 2 × [750 + (190/500)² × 5410] = 2 × 1531.2 = 3062.9 W. Two transformers are better — losses are least, saving 812.4 W. b) Stator copper loss at no load = 3 × (14.5/√3)² × 0.233 = 48.985 W. Fixed losses = 890 − 48.985 = 841 W.
a) Compare total transformer losses (no-load + load-proportional copper loss) for single vs paralleled operation. b) Fixed (iron + friction + windage) losses = no-load input power minus no-load stator copper loss.
📖 §4.7/§4.8 COP vs temperatures (b,c cross-chapter)

6. a) What is the impact of condensing temperature and evaporator temperature on the COP of a refrigeration system? b) Why is it beneficial to operate induction motors in star mode at loads below 50% of rated capacity? c) In a throttle valve-controlled pumping system with oversized pump, name any 3 solutions for improving energy efficiency.

Model answer: a) COP increases with reduction in condensing temperature and with rise in evaporator temperature. b) For motors that consistently operate below 50% of rated capacity, operating in star mode (re-configuring the three phases at the terminal box) reduces voltage by a factor of √3; motor output falls to one-third of the delta value, but performance characteristics as a function of load remain unchanged, so full-load operation in star gives higher efficiency and power factor than partial-load operation in delta. This is only possible where the torque-speed requirement is lower at reduced load. c) Any three of: trim impeller, fit a smaller impeller, install a variable speed drive, use a two-speed motor, use a lower rpm motor.
a) Lower lift (lower condensing, higher evaporator temp) improves COP. b) Star mode reduces applied voltage to better match part-load and improve efficiency/PF. c) Standard remedies for oversized throttle-controlled pumps.
📖 §7.2 Cooling Tower Performance (i)–(iv) Range, Approach, Effectiveness, Capacity; §7.3 Efficient System Operation

7. a) Define Range, approach and effectiveness in cooling tower operation. b) An induced draft cooling tower is designed for a range of 8°C. The energy auditor finds the operating range as 2°C. What could be the reasons for such a situation?

Model answer: a) Range = difference between cooling tower water inlet and outlet temperature. Approach = difference between cooling tower outlet cold water temperature and ambient wet bulb temperature (a better indicator of performance). Effectiveness (%) = ratio of range to the ideal range = Range/(Range + Approach). b) Possible reasons: excess cooling water flow rate; reduced heat load from the process; some cooling tower cell fans switched off; poor approach due to high humidity; nozzles blocked.
Standard cooling-tower definitions plus typical causes of a much lower-than-design operating range.
📖 §4.7 TR formula & COP

8. In an alkali chemical plant, salt brine flowing at 18 m3/hr is cooled from 12°C to 7°C using chilled water. The chiller compressor motor draws 31 kW and total input power to allied accessories is 16 kW. Motor operating efficiency is 90%. Brine density is 1.2 kg/litre and specific heat capacity is 0.97 kCal/kg°C. a) What is the refrigeration load (TR) imposed by the brine cooling? b) What is the COP of the refrigeration compressor? c) What is the overall specific power consumption in kW/TR?

Model answer: a) TR = Q × Cp × (Ti−To)/3024 = (18,000 × 1.2 × 0.97 × (12−7))/3024 = 34.64 TR. b) COP = (3.516 × TR)/(power input to compressor) = 3.516 × 34.64/(31 × 0.9) = 4.365. c) Overall specific power consumption = (31 + 16)/34.64 = 47/34.64 = 1.3568 kW/TR.
a) Refrigeration load from mass flow × specific heat × temp drop / 3024. b) COP converting TR to kW via 3.516 kW/TR over shaft power. c) Total electrical input over refrigeration load.
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