Equipment and Plant Design (ED/PD) Flashcards
The ratio of shear stress to shear strain is called
Shear modulus
A material that is seldom used for pressure vessel construction
Rimmed steel
Fresh water carrying pipelines in chemical industries are colored with _____ color.
Sea green
25% cut segmental baffle means that the baffle
Height is 75% of the I.D of the shell
Liquid/petroleum fuel storage tanks are built underground, when the storage capacity is less than ____ kiloliters.
45
Le/D for fully open globe valve may be around
300
Lug support is
A. The most suitable for thick vertical vessel
B. Same as bracket support
C. Provided usually for vessels of much smaller height than skirt supported vessels
D. A,b,c
D. A,b,c
With increase in the number of shell passes, the value of FT
Increases
Holes of sieve tray are arranged in triangular pitch of _____ times the hole diameter.
2.5 to 5
In cae of a shell and tube heat exchanger, the min. shell thickness for carbon steel depends on shell diameter abd is in the range of ____ mm.
5-11
The stress developed in a material without any permanent set is called the
Elastic limit
In a shell and tube heat exchanger, the ‘tube pitch’ is defined as the
A. O.D of the tube for square pitch
B. Shortest distance between two adjacent tube holes
C. Shortest centre to centre distance between adjacent tubes
D. None of these
C. Shortest centre to centre distance between adjacent tubes
Which of the following is not a valid assumption in continuous binary distillation for calculating the number of equilibrium stages by Mc-Cabe-Thiele method?
A. Sensible heat changes for vapor and liquid are negligibly small
B. Reflux is not a saturated liquid
C. Molar latent heat of the two components are equal
D. None of these
B. Reflux is not a saturated liquid
The value of fouling factor depends upon the
A. Characteristics of process fluid
B. Velocity of process fluid containing suspended solids
C. Suspended solids in the fluid
D. A, b, c
D. A, b, c
In the case of the bubble cap distillation column of a diameter greater than 1.2m, the cap diameter is roughly about _____ cm.
10
Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about ____ times, that in a 1-1 heat exchanger having the same size and number of tubes and operated at the same liquid flow rate.
8
To keep the power input constant for a stirred vessel operating under fully developed turbulent flow conditions (constant power number), if the impeller diameter is increased by 20%, the impeller speed should be decreased by a factor of
(1.2)^5/3
In a heat exchanger, shell side fluid velocity can be changed by changing the tube
A. Layout
B. Pitch
C. Both a and b
D. Neither a and b
C. Both a and b
It is where the maximum tensile strength occur in a thick cylindrical vessel subjected to internal pressure
At the inner surface
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than
0.80
A rivetted joint does not fail by ____ of rivets
0.55
Triangular pitch tube layout as compared to the square pitch in a shell and tube heat exchanger
A. Permits the use of less tubes in a given shell diameter
B. Facilitates comparatively easier external cleaning because of large clearance
C. Permits the use of more tubes in a given shell diameter
D. Both b and c
C. Permits the use of more tubes in a given shell diameter
Bracket supports are the most suitable for supporting ______ vessels
Thick-walled vertical
In a multi-pass shell and tube heat exchanger, the shell side cross flow area does not depend upon
A. Baffle spacing
B. Clearance
C. Pitch
D. None of these
D. None of these