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Chemical Engineering · all questions

Heat Transfer
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With increase in temperature, the total emissivity of conductors

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For a fluid flowing in an annulus space, the wetted perimeter for heat transfer and pressure drop are

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Dietus-Boelter equation used for the determination of heat transfer co-efficient is valid

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The outlet temperature of cooling water in a heat exchanger is generally not allowed to exceed above 50°C in industrial practice mainly to avoid

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The variation of thermal conductivity of a metal with temperature is often correlated using an expression of the form K = K0 + at. where, K is the thermal conductivity and T is the temperature (in °K). The units of 'a' in SI system will be

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The inside heat transfer co-efficient in case of turbulent flow of liquid in the tube side in a 1-2 shell and tube heat exchanger is increased by __________ times, when the number of tube passes is increased to 8.

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Electromagnetic radiations propagate in vacuum with a velocity of __________ metre/second.

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Which of the following is generally considered as opaque surface towards radiations?

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The characteristic dimensionless groups for heat transfer to a fluid flowing through a pipe in laminar flow are

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Heat transfer by __________ may not necessarily require the presence of a medium.

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Which is the most suitable for cold viscous feed?

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In a forward feed multiple effect evaporator unit

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In a shell and tube type heat exchanger, the floating tube bundle heat arrangement is used

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What is the unit of thermal conductivity?

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Multiple effect evaporators are commonly used in the manufacture of P. Paper Q. Superphosphate R. Sugar S. Fats

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Nusselt number is a function of Prandtl number and __________ number of fluid in natural convection heat transfer.

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In a heat exchanger with steam outside the tubes, a liquid gets heated to 45°C, when its flow velocity in the tubes is 2 m/s. If the flow velocity is reduced to 1 m/s, other things remaining the same, the temperature of the exit liquid will be

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The left face of a one dimensional slab of thickness 0.2 m is maintained at 80°C and the right face is exposed to air at 30°C. The thermal conductivity of the slab is 1.2 W/m.K and the heat transfer co-efficient from the right face is 10 W/m2.K. At steady state, the temperature of the right face in °C is

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

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In forced convection, the Nusselt number is a function of

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