Option A: Admit the feed
Option B: Remove the product
Option C: Facilitate removal of non-condensable gases
Option D: Create vacuum
Correct Answer: Facilitate removal of non-condensable gases ✔
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Option A: Increases
Option B: Decreases
Option C: Remains unchanged
Option D: Increases exponentially
Correct Answer: Decreases ✔
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Option A: Infinity
Option B: Zero
Option C: Same as average heat transfer co-efficient for tube side
Option D: None of these
Correct Answer: Infinity ✔
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Option A: Liquid density
Option B: Liquid viscosity
Option C: Hot surface temperature
Option D: Interfacial tension
Correct Answer: Interfacial tension ✔
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Option A: Type of absorbing surface
Option B: Distance between the heat source and the object receiving the heat
Option C: Surface area and temperature of the heat source
Option D: None of these
Correct Answer: None of these ✔
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Option A: Brinkman number
Option B: Stanton number
Option C: Schmidt number
Option D: Peclet number
Correct Answer: Schmidt number ✔
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Option A: Antoine
Option B: Kopp’s
Option C: Lee’s
Option D: Kistyakowsky
Correct Answer: ✔
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Option A: Temperature distribution is independent of time
Option B: Temperature distribution is dependent on time
Option C: Heat flows in one direction only
Option D: Three dimensional heat flow is concerned
Correct Answer: Temperature distribution is dependent on time ✔
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Option A: Tube thickness
Option B: Cross-sectional area
Option C: Weight per unit length
Option D: None of these
Correct Answer: Cross-sectional area ✔
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Option A: t = 283 s
Option B: t = 356 s
Option C: t = 400 s
Option D: t = 800 s
Correct Answer: t = 800 s ✔
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Option A: 1 to 2
Option B: 5 to 10
Option C: 100 to 500
Option D: 1000 to 2000
Correct Answer: 5 to 10 ✔
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Option A: Same
Option B: Different
Option C: Never different
Option D: Linearly related
Correct Answer: Different ✔
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Option A: 520
Option B: 200
Option C: 400
Option D: 500
Correct Answer: 400 ✔
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Option A: Clean and dirt free
Option B: Smooth clean
Option C: Contaminated cooling
Option D: Polished
Correct Answer: Contaminated cooling ✔
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Option A: Viscosity
Option B: Density
Option C: Thermal conductivity
Option D: Corrosive nature
Correct Answer: Viscosity ✔
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Option A: Decrease
Option B: Increase
Option C: First decrease and then increase
Option D: First increase and then decrease
Correct Answer: First increase and then decrease ✔
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Option A: Feed is introduced in the first effect
Option B: Feed flows from low pressure to high pressure
Option C: No pumps are required between successive effects
Option D: None of these
Correct Answer: Feed flows from low pressure to high pressure ✔
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Option A: Basket type
Option B: Horizontal tube
Option C: Short tube vertical
Option D: Long tube vertical
Correct Answer: Horizontal tube ✔
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Option A: Large scale evaporation of liquor is needed
Option B: Corrosive liquids are to be concentrated
Option C: Fuel is cheaply available
Option D: Evaporation on small scale is to be done
Correct Answer: Large scale evaporation of liquor is needed ✔
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Option A: 1.49
Option B: 1
Option C: 4.88
Option D: None of these
Correct Answer: 1.49 ✔
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Option A: Black & smooth
Option B: Black & rough
Option C: White & smooth
Option D: White & rough
Correct Answer: Black & rough ✔
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Option A: The cooling rate will be the same for the two spheres and hence the two spheres will have
Option B: Both the spheres will emit equal amount of radiation per unit time in the beginning
Option C: Both will absorb equal amount of radiation from the surrounding in the beginning
Option D: Both B. & C.
Correct Answer: D. Both B. & C. ✔
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Option A: Brick
Option B: Air
Option C: Water
Option D: Silver
Correct Answer: Silver ✔
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Option A: Avoid cavitation
Option B: Avoid frequent priming
Option C: Create more suction head
Option D: None of these
Correct Answer: Create more suction head ✔
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Option A: Steam pressure
Option B: Feed temperature
Option C: Number of effect
Option D: Both B. & C.
Correct Answer: D. Both B. & C. ✔
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‘Fouling factor’ used in the design of a multipass shell and tube heat exchanger is a__________?
Option A: Non-dimensional factor
Option B: Factor of safety
Option C: Conversion factor for individual film heat transfer co-efficient to overall heat transfer coefficient
Option D: None of these
Correct Answer: Factor of safety ✔
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Option A: Buffer zone
Option B: Turbulent core
Option C: Both A. and B.
Option D: Viscous sub-layer
Correct Answer: Viscous sub-layer ✔
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Option A: Atmospheric
Option B: Sub-atmospheric
Option C: Negative
Option D: Very high
Correct Answer: Very high ✔
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Option A: Thickness of the wall
Option B: Area of the wall perpendicular to heat flow
Option C: Material of the wall
Option D: Temperature difference between the two surfaces of the wall
Correct Answer: Temperature difference between the two surfaces of the wall ✔
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Option A: High viscosity liquid is to be cooled
Option B: Requirement of heat transfer area is low
Option C: Overall heat transfer co-efficient is very high
Option D: A corrosive liquid is to be heated
Correct Answer: Requirement of heat transfer area is low ✔
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Option A: Decreases
Option B: Increases
Option C: Increases exponentially
Option D: Remain unaffected
Correct Answer: Decreases ✔
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Option A: Decreases
Option B: Increases
Option C: Remains unchanged
Option D: Increases exponentially
Correct Answer: Decreases ✔
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Option A: d2T/dZ2 > 0
Option B: d2T/dZ2 = 0
Option C: d2T/dZ2 < 0
Option D: dT/dZ = 0
Correct Answer: d2T/dZ2 = 0 ✔
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Option A: Resistances in parallel
Option B: Capacitors in series
Option C: Resistances in series
Option D: None of these
Correct Answer: Resistances in series ✔
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Option A: High viscosity
Option B: High co-efficient of thermal expansion
Option C: Low temperature gradients
Option D: Low density change with temperature
Correct Answer: High co-efficient of thermal expansion ✔
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Option A: St = f/2
Option B: St = f/4
Option C: St = 4f
Option D: St = f1/2
Correct Answer: St = f/2 ✔
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Option A: Total condenser
Option B: Vacuum evaporator
Option C: Partial condenser
Option D: Double pipe heat exchanger
Correct Answer: Partial condenser ✔
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Option A: The heat transfer rate is low in view of the large temperature drop
Option B: It is difficult to maintain
Option C: It is not economic
Option D: None of these
Correct Answer: The heat transfer rate is low in view of the large temperature drop ✔
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Option A: Heat sensitive material can be handled
Option B: There is no additional cost of pumping
Option C: Most concentrated liquid is at highest temperature
Option D: Equal heat transfer co-efficients exist in various effects
Correct Answer: Most concentrated liquid is at highest temperature ✔
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Option A: Increases
Option B: Decreases
Option C: Does not affect
Option D: May increase or decrease, depends on the type of baffle
Correct Answer: Increases ✔
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Option A: Increases
Option B: Decreases
Option C: Remains unchanged
Option D: May increase or decrease; depending on temperature
Correct Answer: Increases ✔
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Option A: 3 × 105
Option B: 3 × 108
Option C: 3 × 1010
Option D: 3 × 1012
Correct Answer: 3 × 108 ✔
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Option A: Facilitate cleaning of the exchanger
Option B: Increase the heat transfer area
Option C: Relieve stresses caused by thermal expansion
Option D: Increase log mean temperature gradient
Correct Answer: Relieve stresses caused by thermal expansion ✔
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Option A: Bleed point
Option B: Vent
Option C: Catchall
Option D: Baffle
Correct Answer: Catchall ✔
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Option A: Smaller than
Option B: Greater than
Option C: Equal to
Option D: Not related with
Correct Answer: Smaller than ✔
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Option A: Continues to increase
Option B: Continues to decrease
Option C: Goes through a minimum
Option D: Goes through a maximum
Correct Answer: Goes through a minimum ✔
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Option A: Is a dimensionless quantity
Option B: Does not provide a safety factor for design
Option C: Accounts for additional resistances to heat flow
Option D: None of these
Correct Answer: Accounts for additional resistances to heat flow ✔
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Option A: Remains unchanged
Option B: Increases
Option C: Increases or decreases depending on number of shell passes
Option D: Decreases
Correct Answer: Decreases ✔
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Option A: J/M2°K
Option B: W/m2°K
Option C: W/m°K
Option D: J/m°K
Correct Answer: W/m2°K ✔
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Option A: Double pipe
Option B: Plate fine
Option C: Series and parallel set of shell and tube
Option D: None of these
Correct Answer: Series and parallel set of shell and tube ✔
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Option A: Increases
Option B: Decreases
Option C: Remains unchanged
Option D: May increase or decrease; depends on the solid
Correct Answer: Decreases ✔
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Option A: Get economical temperature difference by using moderate pressure steam
Option B: Facilitate forward feeding in multiple effect evaporation
Option C: Concentrate heat sensitive materials
Option D: Achieve very high concentration of the final product
Correct Answer: Get economical temperature difference by using moderate pressure steam ✔
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Option A: Capacity
Option B: Rate of evaporation
Option C: Economy
Option D: Rate of vaporisation
Correct Answer: Economy ✔
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Option A: Laminar
Option B: Transition
Option C: Both A & B
Option D: Highly turbulent
Correct Answer: Highly turbulent ✔
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Option A: Reynolds number
Option B: Prandtl number
Option C: Grashoff number
Option D: None of these
Correct Answer: Grashoff number ✔
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Option A: C/E
Option B: E/C
Option C: CE
Option D: 1/CE
Correct Answer: C/E ✔
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Option A: Prandtl number
Option B: Grashoff number
Option C: Thermal conductivity
Option D: Viscosity
Correct Answer: Prandtl number ✔
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Option A: 25°C
Option B: 30°C
Option C: 35°C
Option D: 40°C
Correct Answer: 35°C ✔
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Option A: Twice
Option B: Four times
Option C: Square root of
Option D: Square of
Correct Answer: Four times ✔
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Option A: IR
Option B: I2R
Option C: IR2
Option D: I2R2
Correct Answer: I2R ✔
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Option A: Painting the surface black
Option B: Painting the surface white (with aluminium paint)
Option C: Giving the surface a mirror finish
Option D: Roughening the surface
Correct Answer: Painting the surface white (with aluminium paint) ✔
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Option A: Convection
Option B: Radiation
Option C: Conduction
Option D: All A., B. & C.
Correct Answer: Conduction ✔
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Option A: Temperature of the body only
Option B: Wavelength of monochromatic radiation
Option C: Both A. and B.
Option D: Nature of material of body
Correct Answer: Temperature of the body only ✔
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Option A: Film boiling
Option B: Nucleate boiling
Option C: Vapour binding
Option D: None of these
Correct Answer: Nucleate boiling ✔
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Option A: Temperature
Option B: Porosity
Option C: Both A. & B.
Option D: Neither A. nor B.
Correct Answer: C. Both A. & B. ✔
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Option A: Surrounding temperature
Option B: Average temperature of the fin
Option C: Temperature of the fin end
Option D: Constant temperature equal to that of the base
Correct Answer: Constant temperature equal to that of the base ✔
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The actual temperature drop across the heating surface in an evaporator depends on the__________?
Option A: Feed
Option B: Depth of liquid over heating surface
Option C: Pressure difference between steam chest and vapour space
Option D: All A., B. and C.
Correct Answer: D. All A., B. and C. ✔
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Option A: Length
Option B: Area
Option C: Volume
Option D: None of these
Correct Answer: Area ✔
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Option A: Remove condensate from the steam pipelines
Option B: Create vacuum
Option C: Superheat the steam
Option D: None of these
Correct Answer: Create vacuum ✔
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Option A: Vertical heat exchanger with steam on tube side
Option B: Vertical heat exchanger with steam on shell side
Option C: Horizontal heat exchanger with steam on tube side
Option D: Horizontal heat exchanger with steam on shell side
Correct Answer: Vertical heat exchanger with steam on shell side ✔
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Option A: Gases
Option B: Solids
Option C: Liquids
Option D: Both B. and C.
Correct Answer: D. Both B. and C. ✔
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Option A: Isothermal
Option B: Non-isothermal
Option C: Both A. and B.
Option D: Neither A. and B.
Correct Answer: C. Both A. and B. ✔
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Option A: 0.5
Option B: 0.05
Option C: 0.1
Option D: 0.15
Correct Answer: 0.1 ✔
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Option A: √(ΔT1 . ΔT2)
Option B: 2 (ΔT1 . ΔT2)/(ΔT1 + ΔT2)
Option C: 2 (ΔT1 . ΔT2)/(ΔT1 – ΔT2)
Option D: (ΔT1 – ΔT2)/(ΔT1 . ΔT2)
Correct Answer: 2 (ΔT1 . ΔT2)/(ΔT1 + ΔT2) ✔
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Option A: ha = hl
Option B: ha = 2hl
Option C: ha = 0.5 hl
Option D: ha = 0.75 hl
Correct Answer: ha = 2hl ✔
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Option A: (ΔT)1/4
Option B: (ΔT)1/2
Option C: (ΔT)5/4
Option D: (ΔT)3/4
Correct Answer: (ΔT)3/4 ✔
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Option A: Viscosity
Option B: Density
Option C: Thermal conductivity
Option D: Heat capacity
Correct Answer: Density ✔
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Option A: 555
Option B: 55.5
Option C: 0.55
Option D: 0.15
Correct Answer: 0.15 ✔
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Option A: Prandtl
Option B: Nusselt
Option C: Stanton
Option D: Grashoff
Correct Answer: Prandtl ✔
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Option A: Zero
Option B: One
Option C: ∞
Option D: Between 0 and ∞
Correct Answer: Zero ✔
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Option A: 5.6697 × 10-8W/m2.°K4
Option B: 0.1714 × 10-8W/m2.°K4
Option C: 5.6697 × 10-8kcal/m2. °K4
Option D: 0.1714 × 10-8kcal/m2. °K4
Correct Answer: 5.6697 × 10-8W/m2.°K4 ✔
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Option A: 5.6
Option B: 0.025
Option C: 3.5
Option D: 0.0035
Correct Answer: 0.025 ✔
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Option A: Plate type
Option B: Double pipe type with fin on steam side
Option C: Double pipe type with fin on air side
Option D: Shell and tube type
Correct Answer: Double pipe type with fin on air side ✔
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Option A: Agitated film evaporator
Option B: Long tube vertical evaporator
Option C: Open pan evaporator
Option D: None of these
Correct Answer: Long tube vertical evaporator ✔
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Option A: 1000
Option B: 727
Option C: 800
Option D: 1200
Correct Answer: 1000 ✔
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Option A: Increases rapidly with temperature rise
Option B: Decreases rapidly with temperature rise
Option C: In independent of pressure
Option D: Both B. and C.
Correct Answer: Increases rapidly with temperature rise ✔
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Option A: Facilitate the cleaning of outer tube surface
Option B: Enhance turbulence
Option C: Hold the tubes in position
Option D: All A , B & C
Correct Answer: Enhance turbulence ✔
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Steam side heat transfer co-efficient in an evaporator is in the range of __________ kcal/hr.m2°C?
Option A: 10-50
Option B: 100-500
Option C: 1000-1500
Option D: 5000-15000
Correct Answer: 5000-15000 ✔
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Option A: Wavelength of radiation
Option B: Nature of the body
Option C: Temperature of the body
Option D: None of these
Correct Answer: Temperature of the body ✔
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Option A: Δt
Option B: Δt2
Option C: Δt3
Option D: √(Δt)
Correct Answer: Δt ✔
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Option A: 50 -100 Kcal/hr.m2.°C
Option B: 50 -100 W/m2.°K
Option C: 50 -100 BTU/hr. ft.2°F
Option D: 1000 – 1500 BTU/hr. ft.2°F
Correct Answer: 50 -100 BTU/hr. ft.2°F ✔
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Option A: Basket type
Option B: Horizontal tube
Option C: Calandria
Option D: None of these
Correct Answer: Basket type ✔
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Option A: Increases
Option B: Decreases
Option C: Is not affected
Option D: May increase or decrease; depends on the feed
Correct Answer: Decreases ✔
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Option A: Increases the heating area required
Option B: Reduces the economy
Option C: Both A. and B.
Option D: Decreases the heating area required
Correct Answer: C. Both A. and B. ✔
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Option A: Baffle spacing & shell diameter
Option B: Tube diameter & pitch
Option C: Viscosity, density & mass velocity of shell side fluid
Option D: None of these
Correct Answer: None of these ✔
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