Questions 591–600 of 650. Imported answers require independent review unless marked reviewed.

Topic practice 650 questionsPage 60 of 65

Question 6

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The volumetric properties of two gases M and N are described by the generalized compressibility chart which expresses the compressibility factor (

) as a function of reduced pressure and reduced temperature only. The operating pressure (

) and temperature (

) of two gases M and N along with their critical properties (

) are given in the table below.
Gas

(bar)

(K)

(bar)

(K)
M
25
300
75
150
N
75
1000
225
500

and

are the compressibility factor of the gases M and N under the given operating conditions, respectively. The relation between

and

is
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Question 7

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Water is heated at atmospheric pressure from 40°C to 80°C using two different processes. In process I, the heating is done by a source at 80°C. In process II, the water is first heated from 40°C to 60°C by a source at 60°C, and then from 60°C to 80°C by another source at 80°C.
Identify the correct statement.
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Question 8

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In a venturi meter,

and

are the pressure drops corresponding to volumetric flowrates

and

. If

, then

equals
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Question 9

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The thickness of laminar boundary layer over a flat plate varies along the distance from the leading edge of the plate. As the distance increases, the boundary layer thickness
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Question 10

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Which of the following is the correct sequence of equipment for size reduction of solids?
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Question 11

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A gas bubble (gas density

kg/m³; bubble diameter

m) is rising vertically through water (density

kg/m³; viscosity

Pa.s). Force balance on the bubble leads to the following equation,

where

is the velocity of the bubble at any given time

. Assume that the volume of the rising bubble does not change. The value of

m/s².
The terminal rise velocity of the bubble (in cm/s), rounded to 2 decimal places, is ______ cm/s.

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Question 12

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The one-dimensional unsteady heat conduction equation is

where

– temperature,

– time,

– radial position,

– thermal conductivity,

– density, and

– specific heat.
For the cylindrical coordinate system, the value of

in the above equation is
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Question 13

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In a heat exchanger, the inner diameter of a tube is 25 mm and its outer diameter is 30 mm. The overall heat transfer coefficient based on the inner area is 360 W/m²·°C. Then, the overall heat transfer coefficient based on the outer area, rounded to the nearest integer, is ______ W/m²·°C.

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Question 14

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Which of the following conditions are valid at the plat point? P) Density difference between the extract and raffinate phases is zero Q) Interfacial tension between the extract and raffinate phases is zero R) Composition difference between the extract and raffinate phases is zero
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Question 15

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The composition of vapour entering a tray in a distillation column is 0.47. The average composition of the vapour leaving the tray is 0.53. The equilibrium composition of the vapour corresponding to the liquid leaving this tray is 0.52. All the compositions are expressed in mole fraction of the more volatile component.
The Murphree efficiency based on the vapour phase, rounded to the nearest integer, is ______ %.

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