A. 1
B. 2
D. 0.5
A. Average velocity
B. Average flow rate
D. Pressure
A. 15 to 25
C. 2 to 5
D. >25
A. Equal to
B. Not necessarily greater than
D. Less than
A. Less than barometric pressure
B. Less than the vapour pressure of the liquid
C. Equal to the vapour pressure of the liquid
B. BHP required by the pump
C. NPSH required
D. Head of the liquid pumped
A. Turbulent forces
B. Viscous forces
D. Pressure forces
A. Newtons first law of motion
B. Newtons second law of motion
C. Conservation of energy
A. Decreases linearly with V
B. None of these
C. Decreases as V2
A. In case of boundaries experiencing form drag
B. At points of abrupt changes in the flow directions
D. In laminar flow
A. dq/dx = K/q
C. dq/dx = K.q
D. dq/dx = Kq2
A. Is constant along an equipotential surface
C. Relates velocity and pressure
A. 1/M
C. ?M
D. M
A. None of these
B. Skin
C. Disk
B. 2 to 5
C. >25
D. 15 to 25
A. Nitrogen at room temperature
B. Oxygen at room temperature
D. Air at room temperature
A. Facilitate easy dismantling of pipeline for cleaning and maintenance
C. Store a definite quantity of water all the time
A. Ensure intermittent supply of hydraulic pressure
B. Accumulate pressure to increase force
D. Increase the pressure and store/ accumulate it
C. Volume
D. Specific weight
B. Pitot tube
C. Venturimeter
D. Orificemeter
C. M is above G
D. M & G coincide
B. 45 bend
C. 90 bend
D. 30 bend
C. Liquids
D. Mixture of hydrocarbons
A. Orificemeter
C. Pressure gauge
D. Venturimeter
A. Increases exponentially
B. Remains unchanged
C. Increases
B. rpm
C. Impeller blade angle
D. Number of blades in impeller
A. Brinkman
B. Archimedes
D. Euler
D. U-tube manometer
A. Reynolds
B. Pascal
D. Blake-Plummer
A. 325
B. 26
C. 42
B. Increases the work done during suction stroke
C. Decreases the work done during suction stroke
D. Increases the work done during delivery stroke
A. Inertial forces to gravity forces
C. Viscous forces to inertial forces
D. Viscous forces to gravity forces
B. High suction velocity
C. High suction pressure
D. Low barometric pressure
A. Powder & granular solids
B. Low melting point semi-solids
A. Provided to prevent liquid from backing up through the pump when the pump is turned off or
C. Provided in the discharge line
D. Generally a globe valve
E. idently stops running
B. There exists a velocity potential
C. Energy is constant along a streamline
D. Energy is not constant along a streamline
B. Head
C. Efficiency
B. Velocity is uniform at any cross-section
C. Velocity is not zero at the solid surface
D. ers themselves
E. Resistance between the surface & the fluid is lesser as compared to that between the fluid
A. ML-1T-2
C. LT-2
D. L2T-1
B. Submerged weight
C. Submerged volume
D. Own volume
A. Flat near the wall and parabolic in the middle
B. Flat
C. Parabolic
B. f-0.5 = 4.07 loge (NRef)-0.6
C. Both a and b
D. None of these
B. Liquid which it can store
C. Discharge which it can deliver
C. Acid egg
D. Blower
B. Kinematic viscosity
C. Angular velocity
A. Diaphragm
B. Gear
D. Reciprocating
B. 3000
C. 1500
D. 4000
A. 0.33
C. 0.5
D. 1
C. Specific volume
A. 10 KPa
C. 30 KPa
D. 40 KPa
Showing 401 to 450 of 744 mcqs