Explore topic-wise MCQs in Chemical Engineering.

This section includes 425 Mcqs, each offering curated multiple-choice questions to sharpen your Chemical Engineering knowledge and support exam preparation. Choose a topic below to get started.

251.

If Prandtl number is greater than the Schmidt number, then the____________________?

A. Thermal boundary layer lies inside the concentration boundary layer
B. Concentration boundary layer lies inside the thermal boundary layer
C. Thermal & concentration boundary layers are of equal thickness
D. Hydrodynamic (i.e., momentum) boundary layer is thicker than the other two
Answer» B. Concentration boundary layer lies inside the thermal boundary layer
252.

If heat transfer rate varies with the time, it is termed as__________________?

A. Forced convection
B. Steady state conduction
C. Monochromatic radiation
D. None of these
Answer» E.
253.

If h1 = inner film co-efficient and /h2 = outer film co-efficient, then the overall heat transfer co-efficient is________________?

A. Always less than h1
B. Always between h1 and h2
C. Always higher than h2
D. Dependent on metal resistance
Answer» C. Always higher than h2
254.

If average heat transfer co-efficient is ha and the local coefficient at the end of the plate is hl then in case of heat transfer to a fluid flowing over a flat plate, heated over its entire length________________?

A. ha = hl
B. ha = 2hl
C. ha = 0.5 hl
D. ha = 0.75 hl
Answer» C. ha = 0.5 hl
255.

If all the conditions and dimensions are same, then the ratio of velocity through the tubes of a double pass heat exchanger to that through the single pass heat exchanger is_________________?

A. 1
B. 2
C. 1/2
D. 4
Answer» C. 1/2
256.

If air (a non-condensing gas) is present in a condensing vapor stream, it will ______________ the condensation rate of vapor?

A. Increase
B. Decrease
C. Not affect
D. Increase the condensing film co-efficient as well as
Answer» C. Not affect
257.

If a single tube pass heat exchanger is converted to two pass, then for the same flow rate, the pressure drop per unit length in tube side will ________________?

A. Increase by 1.8 times
B. Decrease by 22
C. Increase by 216
D. Remain unchanged
Answer» D. Remain unchanged
258.

Hot water (0.01 m3 /min) enters the tube side of a counter current shell and tube heat exchanger at 80°C and leaves at 50°C. Cold oil (0.05 m3/min) of density 800 kg/m3 and specific heat of 2 kJ/kg.K enters at 20°C. The log mean temperature difference in °C is approximately ?

A. 32
B. 37
C. 45
D. 50
Answer» B. 37
259.

Heat waves_____________________?

A. Cannot pass through vacuum
B. Travel in straight line
C. Can be reflected by a mirror
D. Both B. and C.
Answer» E.
260.

Heat transfer rate per unit area is called_________________?

A. Thermal conductivity
B. Heat flux
C. Heat transfer co-efficient
D. Thermal diffusivity
Answer» C. Heat transfer co-efficient
261.

Heat transfer rate described by Fourier’s law will decrease, if the _____________ increases?

A. Thermal conductivity
B. Thickness
C. Temperature difference
D. Heat transfer area
Answer» C. Temperature difference
262.

Heat transfer occurs by natural convection because change in temperature causes difference in__________________?

A. Viscosity
B. Density
C. Thermal conductivity
D. Heat capacity
Answer» C. Thermal conductivity
263.

Heat transfer in the laminar sub-layer in case of a liquid flowing through a pipe, is mostly by__________________?

A. Eddies current
B. Conduction
C. Convection
D. None of these
Answer» C. Convection
264.

Heat transfer efficiency leading of energy conservation in a heat exchanger can be achieved by____________________?

A. Keeping the heat transfer surface clean
B. Enhancing the fluid pumping rate
C. Increasing the tube length
D. None of these
Answer» B. Enhancing the fluid pumping rate
265.

Heat transfer co-efficient (h1) for liquids increases with__________________?

A. Increasing temperature
B. Decreasing temperature
C. Decreasing Reynolds number
D. None of these
Answer» B. Decreasing temperature
266.

Heat transfer co-efficient (h) for a fluid flowing inside a clean pipe is given by h = 0.023 (K/D) (DVρ/μ)0.8 (CP.μ/k)0.4. This is valid for the value of NRe equal to_______________?

A. 4000
B. > 10000
Answer» C.
267.

Heat transfer co-efficient equation for forced convection, Nu = 0.023 Re 0.8. Pr n, is not valid, if the value of __________________?

A. n = 0.4 is used for heating
B. n = 0.3 is used for cooling
C. Reynolds number for the flow involved is > 10000
D. Reynolds number for the flow involved is < 2100
Answer» E.
268.

Heat transfer by radiation between two bodies at T1 & T2 and in an ambient temperature of Ta°C depends on_____________?

A. T1 – T2
B. T1 – Ta
C. T2 – Ta
D. None of these
Answer» E.
269.

Heat transfer by natural convection is enhanced in system with__________________?

A. High viscosity
B. High co-efficient of thermal expansion
C. Low temperature gradients
D. Low density change with temperature
Answer» C. Low temperature gradients
270.

Heat transfer by ____________ may not necessarily require the presence of a medium?

A. Conduction
B. Natural convection
C. Forced convection
D. Radiation
Answer» E.
271.

Heat transfer by conduction results due to the transfer of free electrons, kinetic energy & vibrational energy from one molecule to another. Conduction heat transfer cannot take place____________________?

A. Between two bodies in physical contact with each other
B. Between two bodies not in physical contact with each other
C. From one part of a body to the another part of the same body
D. Both B & C
Answer» C. From one part of a body to the another part of the same body
272.

Heat transfer by conduction in the turbulent core of a fluid flowing through a heated pipe is negligible, if the value of Prandtl number is_______________?

A. 0.2
B. 0.4
C. 0.6
D. 0.8
Answer» D. 0.8
273.

Heat sensitive materials can be concentrated in an evaporator employing_______________?

A. Vacuum
B. High pressure
C. High residence time
D. None of these
Answer» B. High pressure
274.

Heat produced when a steady state current, I passes through an electrical conductor having resistance, ‘R’ is___________________?

A. IR
B. I2R
C. IR2
D. I2R2
Answer» C. IR2
275.

Heat flux through several resistances in series in analogous to the current flowing through several_____________________?

A. Resistances in parallel
B. Capacitors in series
C. Resistances in series
D. None of these
Answer» D. None of these
276.

Heat flux is the time rate of heat transfer per unit_______________?

A. Length
B. Area
C. Volume
D. None of these
Answer» C. Volume
277.

Heat flux increases with temperature drop beyond the Leiden frost point in the plot of heat flux vs. temperature drop for a boiling liquid, because___________________?

A. Convection becomes important
B. Conduction becomes important
C. Radiation becomes important
D. Sub-cooled boiling occurs
Answer» D. Sub-cooled boiling occurs
278.

Heat flux, as defined in heat flow is analogous to _______________ in electricity flow?

A. Current
B. Voltage
C. Resistance
D. None of these
Answer» B. Voltage
279.

Heat exchangers operating, when the asymptotic range is reached, ?

A. Provide very large heat transfer co-efficient
B. Results in making part of the heating surface inactive
C. Results in abruptly increased velocity
D. None of these
Answer» C. Results in abruptly increased velocity
280.

Heat exchanger tubes are never made of_________________?

A. Plain carbon steel
B. Stainless steel
C. Lead
D. Copper
Answer» D. Copper
281.

_____________ heat exchanger is used for chilling oil to be dewaxed?

A. U-tube
B. Double pipe
C. Fixed tube
D. Floating head
Answer» C. Fixed tube
282.

_____________ heat exchanger is the most suitable, when the temperature of shell side fluid is much higher than that of tube side?

A. Single pass, fixed tube sheet
B. U-tube
C. Three pass, fixed tube sheet
D. None of these
Answer» C. Three pass, fixed tube sheet
283.

Harmonic mean temperature difference is given by_________________?

A. √(ΔT1 . ΔT2)
B. 2 (ΔT1 . ΔT2)/(ΔT1 + ΔT2)
C. 2 (ΔT1 . ΔT2)/(ΔT1 – ΔT2)
D. (ΔT1 – ΔT2)/(ΔT1 . ΔT2)
Answer» C. 2 (ΔT1 . ΔT2)/(ΔT1 – ΔT2)
284.

Grashoff number is given by________________?

A. gD3.β.Δtρ2/μ2
B. gD2βΔtρ/μ2
C. gD2βΔtP2μ
D. gD3βΔtP2/μ
Answer» B. gD2βΔtρ/μ2
285.

Grashoff number, which is defined as g . β (Ts – T∞) ρ2. L3/μ2, is proportional to the ratio of buoyancy force to ____________ force?

A. Viscous
B. Elastic
C. Inertial
D. None of these
Answer» B. Elastic
286.

Graetz number is given by__________________?

A. mCp/kL
B. kL/mCp
C. mCp/kμ
D. kμ/mCp
Answer» B. kL/mCp
287.

Fruit juice (a heat sensitive material) can be concentrated in a ____________ evaporator?

A. Long tube
B. Falling film
C. High pressure
D. None of these
Answer» C. High pressure
288.

Fresh orange juice contains 12% (by weight) solids and the rest water 90% of the fresh juice is sent to an evaporator to remove water and subsequently mixed with the remaining 10% of fresh juice. The resultant product contains 40% solids. The kg of water removed from 1 kg fresh juice is__________________?

A. 0.4
B. 0.5
C. 0.6
D. 0.7
Answer» E.
289.

Fqra cold viscous feed, backward feed gives _____________ than forward feed?

A. A higher capacity
B. A lower capacity
C. Lower economy
D. None of these
Answer» B. A lower capacity
290.

Fourier’s law of heat conduction applies to _____________ surfaces?

A. Isothermal
B. Non-isothermal
C. Both A. and B.
D. Neither A. and B.
Answer» D. Neither A. and B.
291.

Fourier’s law applies to the heat transfer by__________________?

A. Convection
B. Radiation
C. Conduction
D. All A., B. & C.
Answer» D. All A., B. & C.
292.

Fouling factor_____________________?

A. Is a dimensionless quantity
B. Does not provide a safety factor for design
C. Accounts for additional resistances to heat flow
D. None of these
Answer» D. None of these
293.

‘Fouling factor’ used in the design of a multipass shell and tube heat exchanger is a_____________________?

A. Non-dimensional factor
B. Factor of safety
C. Conversion factor for individual film heat transfer co-efficient to overall heat transfer coefficient
D. None of these
Answer» C. Conversion factor for individual film heat transfer co-efficient to overall heat transfer coefficient
294.

Fouling factor for a heat exchanger is given by (where, U1 = heat transfer co-efficient of dirty surface U2 = heat transfer co-efficient of clean surface) ?

A. U1 – U2
B. 1/U1 – 1/U2
C. 1/U2 – 1/U1
D. U2 – U1
Answer» C. 1/U2 – 1/U1
295.

Forced circulation evaporators are useful for the concentration of viscous, salting and scale forming liquors. Which of the following is a forced circulation evaporator ?

A. Long vertical evaporator
B. Horizontal tube evaporator
C. Agitated film evaporator
D. Calandria vertical tube evaporator
Answer» D. Calandria vertical tube evaporator
296.

Forced circulation evaporators are normally used for concentrating liquids having ___________________?

A. Scaling characteristics
B. High viscosity
C. Both A. & B.
D. Neither A. nor B.
Answer» D. Neither A. nor B.
297.

For what value of Prandtl number, St = f/2 ?

A. 1.5
B. 1
C. > 1
D. < 1
Answer» C. > 1
298.

For turbulent flow in a tube, the heat transfer co-efficient is obtained from the Dittus- Boelter correlation. If the tube diameter is halved and the flow rate is doubled, then the heat transfer co-efficient will change by a factor of________________?

A. 1
B. 1.74
C. 6.1
D. 37
Answer» D. 37
299.

For the same heat load and mass flow rate in the tube side of a shell and tube heat exchanger, one may use multipass on the tube side, because it__________________?

A. Decreases the pressure drop
B. Decreases the outlet temperature of cooling medium
C. Increases the overall heat transfer coefficient
D. None of these
Answer» D. None of these
300.

For the same heat transfer area and the terminal conditions, the ratio of the capacities of a single effect evaporator to a triple effect evaporator is_________________?

A. 3
B. 0.33
C. 1
D. 1.33
Answer» D. 1.33