Question 1 of 78Classification of Fluids and Fluid Properties
A fluid is defined as a substance that
Ahas a definite shape and volume at all temperatures
Boffers no resistance whatsoever to deformation
Ccannot be compressed under any circumstances
Ddeforms continuously under the action of any shear stress, however small
Answer is hidden
Question 2 of 78Classification of Fluids and Fluid Properties
An ideal fluid is one which is
Ahighly viscous but incompressible
Bcompressible but frictionless in pipes only
Cinviscid and incompressible
DNewtonian at all shear rates but viscous
Answer is hidden
Question 3 of 78Classification of Fluids and Fluid Properties
The SI unit of dynamic viscosity is
Asquare metre per second
Bnewton per metre
Cpascal second
Dkilogram per cubic metre
Answer is hidden
Question 4 of 78Classification of Fluids and Fluid Properties
A10 pascal second
B0.1 pascal second
C0.001 pascal second
D1 pascal second
Answer is hidden
Question 5 of 78Classification of Fluids and Fluid Properties
With an increase in temperature, the viscosity of a liquid and that of a gas respectively
Aincreases and increases
Bincreases and decreases
Cdecreases and increases
Ddecreases and decreases
Answer is hidden
Question 6 of 78Classification of Fluids and Fluid Properties
A fluid whose apparent viscosity decreases with increasing shear rate is called
Apseudoplastic
Brheopectic
Cdilatant
DBingham plastic
Answer is hidden
Question 7 of 78Classification of Fluids and Fluid Properties
Toothpaste and drilling mud, which do not flow until a certain minimum shear stress is exceeded, are examples of
ABingham plastics
Bthixotropic fluids only
Cdilatant fluids
Dideal fluids
Answer is hidden
Question 8 of 78Classification of Fluids and Fluid Properties
A fluid whose apparent viscosity decreases with time at a constant rate of shear is
Apseudoplastic
Brheopectic
Cdilatant
Dthixotropic
Answer is hidden
Question 9 of 78Classification of Fluids and Fluid Properties
Kinematic viscosity is defined as
Adynamic viscosity multiplied by density
Bdynamic viscosity divided by density
Cdensity divided by dynamic viscosity
Dshear stress divided by shear rate
Answer is hidden
Question 10 of 78Classification of Fluids and Fluid Properties
The excess pressure inside a soap bubble of radius R and surface tension sigma is
Answer is hidden
Question 11 of 78Classification of Fluids and Fluid Properties
Capillary rise in a small vertical tube is
Aindependent of the tube radius
Bproportional to the square of the tube radius
Cinversely proportional to the tube radius
Ddirectly proportional to the tube radius
Answer is hidden
Question 12 of 78Classification of Fluids and Fluid Properties
Pascal's law states that the pressure at a point in a fluid at rest
Ais the same in all directions
Bdepends on the shape of the containing vessel
Cincreases in the direction of flow
Dis greatest in the horizontal direction
Answer is hidden
Question 13 of 78Classification of Fluids and Fluid Properties
For a U-tube manometer with manometric fluid of density rho-m, process fluid of density rho and reading R, the pressure difference is
ARg(ρm + ρ)
BRgρm
CRgρ
DRg(ρm − ρ)
Answer is hidden
Question 14 of 78Fluid Statics and Kinematics of Fluid Flow
The centre of pressure on a plane surface submerged in a liquid always lies
Aabove the centroid of the surface
Bexactly at the centroid of the surface
Cbelow the centroid of the surface
Dat the top edge of the surface
Answer is hidden
Question 15 of 78Fluid Statics and Kinematics of Fluid Flow
A floating body is in stable equilibrium when
Athe metacentre lies above the centre of gravity
Bthe metacentre lies below the centre of gravity
Cthe centre of buoyancy coincides with the centre of gravity
Dthe metacentric height is zero
Answer is hidden
Question 16 of 78Fluid Statics and Kinematics of Fluid Flow
In steady flow, streamlines, pathlines and streaklines are
Aidentical only in turbulent flow
Bdifferent in every case
Cidentical to one another
Dalways mutually perpendicular
Answer is hidden
Question 17 of 78Fluid Statics and Kinematics of Fluid Flow
For laminar flow in a circular pipe, the ratio of maximum to average velocity is
Answer is hidden
Question 18 of 78Fluid Statics and Kinematics of Fluid Flow
According to the Hagen-Poiseuille equation, for a fixed pressure drop the volumetric flow rate through a pipe varies as
Athe square of the diameter
Bthe square root of the diameter
Cthe diameter
Dthe fourth power of the diameter
Answer is hidden
Question 19 of 78Fluid Statics and Kinematics of Fluid Flow
The velocity potential function exists only when the flow is
Arotational
Bturbulent
Ccompressible
Dirrotational
Answer is hidden
Question 20 of 78Fluid Statics and Kinematics of Fluid Flow
The stream function is defined for
Athree-dimensional flow only
Btwo-dimensional incompressible flow, rotational or irrotational
Cirrotational flow only
Dcompressible flow only
Answer is hidden
Question 21 of 78Fluid Statics and Kinematics of Fluid Flow
Boundary layer separation occurs because of
Aa favourable pressure gradient
Ban increase in fluid viscosity downstream
Can adverse pressure gradient along the flow direction
Dthe no-slip condition alone
Answer is hidden
Question 22 of 78Fluid Statics and Kinematics of Fluid Flow
Bernoulli's equation in its classical form is NOT applicable when
Athe flow is along a single streamline
Bthe flow is steady and incompressible
Cthe fluid is viscous and friction losses are significant
Dthe fluid density is constant
Answer is hidden
Question 23 of 78Fluid Statics and Kinematics of Fluid Flow
The kinetic energy correction factor for fully developed laminar flow in a pipe is
Answer is hidden
Question 24 of 78Fluid Statics and Kinematics of Fluid Flow
Compressibility effects may normally be neglected when the Mach number is below about
Answer is hidden
Question 25 of 78Fluid Statics and Kinematics of Fluid Flow
In a converging-diverging nozzle operating with supersonic exit flow, sonic velocity is reached
Aat the nozzle exit
Bat the throat
Cin the converging section before the throat
Dat the nozzle inlet
Answer is hidden
Question 26 of 78Fluid Statics and Kinematics of Fluid Flow
According to the Buckingham pi theorem, a problem involving 7 variables and 3 fundamental dimensions can be described by
A10 dimensionless groups
B4 dimensionless groups
C3 dimensionless groups
D7 dimensionless groups
Answer is hidden
Question 27 of 78Internal and External Fluid Flow, Flow Measurement, Pumping and Agitation
The Darcy friction factor is related to the Fanning friction factor by
AfDarcy = 0.25 fFanning
BfDarcy = fFanning
CfDarcy = 2 fFanning
DfDarcy = 4 fFanning
Answer is hidden
Question 28 of 78Internal and External Fluid Flow, Flow Measurement, Pumping and Agitation
For laminar flow in a pipe, the friction factor depends on
Aboth Reynolds number and relative roughness
Bneither of these
CReynolds number only
Drelative roughness only
Answer is hidden
Question 29 of 78Internal and External Fluid Flow, Flow Measurement, Pumping and Agitation
In fully developed rough-pipe turbulent flow, the friction factor is
Aconstant for all pipes
Bproportional to Reynolds number
Ca function of relative roughness alone and independent of Reynolds number
Da function of Reynolds number alone
Answer is hidden
Question 30 of 78Internal and External Fluid Flow, Flow Measurement, Pumping and Agitation
The equivalent diameter for flow through an annulus of outer diameter Do and inner diameter Di is
ADo + Di
B(Do − Di)/2
CDo − Di
DDoDi/(Do + Di)
Answer is hidden
Question 31 of 78Internal and External Fluid Flow, Flow Measurement, Pumping and Agitation
The loss coefficient K for a pipe discharging into a large reservoir is approximately
Answer is hidden
Question 32 of 78Internal and External Fluid Flow, Flow Measurement, Pumping and Agitation
Which valve, when fully open, offers the least resistance to flow?
ADiaphragm valve
BGlobe valve
CCheck valve
DGate valve
Answer is hidden
Question 33 of 78Internal and External Fluid Flow, Flow Measurement, Pumping and Agitation
In a venturi meter compared with an orifice meter of the same throat ratio, the permanent pressure loss is
Athe same, since both are head meters
Bzero in both cases
Cmuch higher, because the throat is longer
Dmuch lower, because of the gradual divergent section
Answer is hidden
Question 34 of 78Internal and External Fluid Flow, Flow Measurement, Pumping and Agitation
In a head-type flow meter, the flow rate is proportional to
Athe logarithm of the differential pressure
Bthe square root of the differential pressure
Cthe differential pressure
Dthe square of the differential pressure
Answer is hidden
Question 35 of 78Internal and External Fluid Flow, Flow Measurement, Pumping and Agitation
A rotameter is classified as a
Apositive displacement meter
Bvelocity-probe meter
Cconstant-area meter operating at variable pressure drop
Dvariable-area meter operating at constant pressure drop
Answer is hidden
Question 36 of 78Internal and External Fluid Flow, Flow Measurement, Pumping and Agitation
A Pitot tube is used to measure
Athe mass flow rate directly
Bthe viscosity of the fluid
Cthe total volumetric flow rate directly
Dthe velocity of flow at a point
Answer is hidden
Question 37 of 78Internal and External Fluid Flow, Flow Measurement, Pumping and Agitation
If the speed of a centrifugal pump is doubled, the power required changes by a factor of
Answer is hidden
Question 38 of 78Internal and External Fluid Flow, Flow Measurement, Pumping and Agitation
Cavitation in a centrifugal pump can be avoided by ensuring that
Athe available NPSH exceeds the required NPSH
Bthe discharge head is as high as possible
Cthe suction line is made as long and narrow as possible
Dthe pump is placed well above the liquid level
Answer is hidden
Question 39 of 78Internal and External Fluid Flow, Flow Measurement, Pumping and Agitation
In a fully baffled agitated vessel operating in the turbulent regime, the power number is
Ainversely proportional to Reynolds number
Bessentially constant and independent of Reynolds number
Cproportional to the Froude number
Dproportional to Reynolds number
Answer is hidden
Question 40 of 78Solids Characterization, Size Reduction and Conveying
The sphericity of a cube is approximately
Answer is hidden
Question 41 of 78Solids Characterization, Size Reduction and Conveying
In the Tyler standard screen series, successive screen apertures are in the ratio of
A10
Bthe square root of 2
Cthe fourth root of 2 always
D2
Answer is hidden
Question 42 of 78Solids Characterization, Size Reduction and Conveying
A material described as minus 14 plus 20 mesh is one which
Apassed through a 20-mesh screen and was retained on a 14-mesh screen
Bpassed through a 14-mesh screen and was retained on a 20-mesh screen
Cpassed through both screens
Dwas retained on both screens
Answer is hidden
Question 43 of 78Solids Characterization, Size Reduction and Conveying
Rittinger's law of crushing states that the energy required is proportional to
Athe new crack length produced
Bthe size reduction ratio
Cthe square of the feed diameter
Dthe new surface area created
Answer is hidden
Question 44 of 78Solids Characterization, Size Reduction and Conveying
Kick's law is most applicable to
Aclassification of fines
Bultrafine grinding
Ccoarse crushing of large feed
Dintermediate grinding
Answer is hidden
Question 45 of 78Solids Characterization, Size Reduction and Conveying
The Bond work index is defined as the energy required to reduce a very large feed to a product in which 80 per cent passes
A1 millimetre
B74 micrometres
C100 micrometres
D10 micrometres
Answer is hidden
Question 46 of 78Solids Characterization, Size Reduction and Conveying
If a ball mill is operated at or above its critical speed
Agrinding efficiency reaches its maximum
Bthe balls centrifuge against the shell and grinding effectively ceases
Cthe product becomes extremely fine
Dthe power consumption falls to zero
Answer is hidden
Question 47 of 78Solids Characterization, Size Reduction and Conveying
The angle of nip in a roll crusher must not exceed
Ahalf the angle of friction
Bfour times the angle of friction
Ctwice the angle of friction
Dthe angle of friction
Answer is hidden
Question 48 of 78Solids Characterization, Size Reduction and Conveying
Which of the following mills produces an ultrafine product with essentially no moving parts in the grinding zone?
AFluid energy (jet) mill
BJaw crusher
CBall mill
DHammer mill
Answer is hidden
Question 49 of 78Solids Characterization, Size Reduction and Conveying
Compared with dry grinding, wet grinding generally
Arequires less power per tonne and produces no dust
Brequires more power per tonne and produces more dust
Ccauses less wear on the grinding media
Dcannot produce a fine product
Answer is hidden
Question 50 of 78Solids Characterization, Size Reduction and Conveying
Closed-circuit grinding is preferred to open-circuit grinding because it
Aalways produces a coarser product
Brequires no recycle stream
Celiminates the need for a classifier
Dreturns oversize to the mill and avoids over-grinding of acceptable material
Answer is hidden
Question 51 of 78Solids Characterization, Size Reduction and Conveying
A bucket elevator is used primarily for
Asize reduction of friable solids
Bvertical lifting of free-flowing bulk solids
Cpneumatic transport of fine powders
Dlong horizontal transport of large tonnages
Answer is hidden
Question 52 of 78Solids Characterization, Size Reduction and Conveying
In dilute-phase pneumatic conveying, the solids are
Acarried as a dense moving bed
Btransported entirely by gravity
Cmoved as plugs at low velocity and high loading
Dfully suspended in a high-velocity gas stream at low solids loading
Answer is hidden
Question 53 of 78Screening and Other Separation Methods
Screening separates particles on the basis of
Asize alone
Bsurface wettability
Cdensity alone
Delectrical conductivity
Answer is hidden
Question 54 of 78Screening and Other Separation Methods
The effectiveness of a screen based on the undersize is given by
AB xB/(F xF)
BB xB/(D xD)
CF xF/(B xB)
DD xD/(F xF)
Answer is hidden
Question 55 of 78Screening and Other Separation Methods
As the feed rate to a screen is increased, its capacity and effectiveness respectively
Adecrease and decrease
Bdecrease and increase
Cincrease and increase
Dincrease and decrease
Answer is hidden
Question 56 of 78Screening and Other Separation Methods
Blinding of a screen refers to
Awear of the screen wires by abrasion
Bexcessive vibration of the deck
Coverflow of the feed at the discharge end
Dplugging of the apertures by near-mesh or sticky particles
Answer is hidden
Question 57 of 78Screening and Other Separation Methods
In a differential screen analysis, the number of particles per unit mass in a size interval varies as
Answer is hidden
Question 58 of 78Screening and Other Separation Methods
The volume-surface or Sauter mean diameter is calculated as
AΣ(xi/Dpi)
B1/Σ(xiDpi)
C1/Σ(xi/Dpi)
DΣ(xiDpi)
Answer is hidden
Question 59 of 78Screening and Other Separation Methods
Elutriation separates particles on the basis of
Aparticle shape only
Bterminal settling velocity in an upward fluid stream
Csurface wettability
Dmagnetic susceptibility
Answer is hidden
Question 60 of 78Screening and Other Separation Methods
Froth flotation separates minerals principally by differences in
Asurface wettability
Belectrical conductivity
Cparticle size
Dspecific gravity
Answer is hidden
Question 61 of 78Screening and Other Separation Methods
In froth flotation, the reagent whose function is to make the mineral surface hydrophobic is the
Adepressant
BpH regulator
Ccollector
Dfrother
Answer is hidden
Question 62 of 78Screening and Other Separation Methods
Copper sulphate added to a flotation circuit to make sphalerite respond to a xanthate collector acts as
Aan activator
Ba depressant
Ca collector
Da frother
Answer is hidden
Question 63 of 78Screening and Other Separation Methods
Jigging separates particles principally on the basis of
Asurface charge
Bdensity difference under a pulsating fluid current
Caperture size
Dmagnetic properties
Answer is hidden
Question 64 of 78Screening and Other Separation Methods
Electrostatic separation of beach sands exploits differences in
Aelectrical conductivity of the minerals
Bsurface tension
Cmelting point
Dmagnetic susceptibility
Answer is hidden
Question 65 of 78Screening and Other Separation Methods
Compared with free settling, hindered settling gives
Alower velocities and less sensitivity to density
Bhigher settling velocities and no change in sensitivity
Cidentical velocities in all cases
Dlower settling velocities but greater sensitivity to density differences
Answer is hidden
Question 66 of 78Sedimentation, Fluidization and Filtration
According to Stokes' law, the terminal settling velocity of a small spherical particle is proportional to
Athe square of the particle diameter
Bthe cube of the particle diameter
Cthe particle diameter
Dthe square root of the particle diameter
Answer is hidden
Question 67 of 78Sedimentation, Fluidization and Filtration
Stokes' law for settling is valid when the particle Reynolds number is
Aless than about 1
Bgreater than 200 000
Cgreater than 1000
Dbetween 1 and 1000
Answer is hidden
Question 68 of 78Sedimentation, Fluidization and Filtration
In the Newton's law region of settling, the drag coefficient is approximately
A24/Re
B18.5/Re⁰.6
Cproportional to Reynolds number
D0.44 and nearly independent of Reynolds number
Answer is hidden
Question 69 of 78Sedimentation, Fluidization and Filtration
The purpose of adding alum to a dilute suspension before sedimentation is to
Aincrease the viscosity of the liquid
Bdissolve the suspended solids completely
Cdestabilise the fine particles so that they aggregate into faster-settling flocs
Draise the density of the liquid above that of the solids
Answer is hidden
Question 70 of 78Sedimentation, Fluidization and Filtration
In a continuous thickener, the required cross-sectional area is determined by
Athe diameter of the feed pipe
Bthe density of the overflow liquid
Cthe compression time of the sediment
Dthe settling rate of the most difficult concentration layer
Answer is hidden
Question 71 of 78Sedimentation, Fluidization and Filtration
At the minimum fluidization velocity, the pressure drop across the bed equals
Azero
Btwice the weight of the bed per unit area
Cthe buoyed weight of the bed per unit cross-sectional area
Dthe dynamic pressure of the fluid
Answer is hidden
Question 72 of 78Sedimentation, Fluidization and Filtration
As the fluid velocity is increased beyond the minimum fluidization velocity, the pressure drop across the bed
Aincreases linearly with velocity
Bfalls rapidly to zero
Cincreases with the square of the velocity
Dremains essentially constant while the bed expands
Answer is hidden
Question 73 of 78Sedimentation, Fluidization and Filtration
The Ergun equation for flow through a packed bed contains
Aa single term proportional to velocity
Ba term proportional to the cube of velocity
Ca single term proportional to velocity squared
Da viscous term proportional to velocity and an inertial term proportional to velocity squared
Answer is hidden
Question 74 of 78Sedimentation, Fluidization and Filtration
Gas-solid fluidization in which the gas passes through the bed as bubbles within a dense emulsion phase is called
Aparticulate fluidization
Bspouting
Caggregative or bubbling fluidization
Dhomogeneous fluidization
Answer is hidden
Question 75 of 78Sedimentation, Fluidization and Filtration
The upper limit of the operating velocity range for a fluidized bed is set by
Athe speed of sound in the gas
Bthe bubble rise velocity
Cthe terminal settling velocity of the particles
Dthe minimum fluidization velocity
Answer is hidden
Question 76 of 78Sedimentation, Fluidization and Filtration
In constant-pressure filtration, a plot of t/V against V yields a straight line whose slope is proportional to
Athe reciprocal of the filter area
Bthe filter medium resistance
Cthe filtrate viscosity only
Dthe specific cake resistance
Answer is hidden
Question 77 of 78Sedimentation, Fluidization and Filtration
For a compressible filter cake, doubling the applied pressure difference
Aexactly doubles the filtration rate
Bquadruples the filtration rate
Calways stops filtration completely
Dincreases the filtration rate by less than a factor of two
Answer is hidden
Question 78 of 78Sedimentation, Fluidization and Filtration
The correct sequence of zones encountered by a point on the surface of a rotary drum vacuum filter during one revolution is
Adischarge, drying, washing, cake formation
Bwashing, cake formation, discharge, drying
Cdrying, cake formation, washing, discharge
Dcake formation, washing, drying, discharge
Answer is hidden