Question 1 of 78Introduction to Process Control, Modelling and Controller Modes
The primary objective of a process control system is
Aelimination of all measurement error
Bmaximisation of production rate
Cthe safety of personnel, the plant and the environment
Dminimisation of capital cost
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Question 2 of 78Introduction to Process Control, Modelling and Controller Modes
A control problem in which the set point is held constant and the controller must counteract disturbances is called
Aa regulatory problem
Ba servo problem
Ca feedforward problem
Dan open-loop problem
Answer is hidden
Question 3 of 78Introduction to Process Control, Modelling and Controller Modes
The proportional band of a controller is related to its gain by
APB = 100Kc
BPB = Kc
CPB = Kc/100
DPB = 100/Kc
Answer is hidden
Question 4 of 78Introduction to Process Control, Modelling and Controller Modes
A purely proportional controller always leaves a steady-state offset because
Ait saturates at the set point
Ba non-zero error is required to hold the controller output away from its bias value
Cits gain is always too low
Dit responds only to the rate of change of error
Answer is hidden
Question 5 of 78Introduction to Process Control, Modelling and Controller Modes
Increasing the gain of a proportional controller will
Ahave no effect on the offset
Breduce the offset but never eliminate it, and eventually cause instability
Celiminate the offset completely
Dincrease the offset
Answer is hidden
Question 6 of 78Introduction to Process Control, Modelling and Controller Modes
Integral action in a controller is used principally to
Areduce the effect of measurement noise
Banticipate future errors
Cspeed up the initial response
Deliminate steady-state offset
Answer is hidden
Question 7 of 78Introduction to Process Control, Modelling and Controller Modes
Reset windup in a PI controller occurs when
Athe measurement signal becomes noisy
Bthe derivative gain is set too high
Cthe set point is changed too slowly
Da sustained error saturates the final control element while the integral term continues to accumulate
Answer is hidden
Question 8 of 78Introduction to Process Control, Modelling and Controller Modes
Derivative action cannot be used alone as a control mode because
Ait eliminates offset too quickly
Bit cannot be implemented in hardware
Cit produces no output when the error is constant, however large that error may be
Dit always makes the loop unstable
Answer is hidden
Question 9 of 78Introduction to Process Control, Modelling and Controller Modes
Derivative action is generally avoided on flow control loops because
Aflow loops have no offset
Bflow measurements are noisy and differentiation amplifies the noise
Cderivative action cannot handle liquids
Dflow loops respond too slowly
Answer is hidden
Question 10 of 78Introduction to Process Control, Modelling and Controller Modes
An air-to-open control valve will, on failure of the instrument air supply,
Aclose
Boscillate
Cremain in its last position
Dopen fully
Answer is hidden
Question 11 of 78Introduction to Process Control, Modelling and Controller Modes
For cooling water supplied to an exothermic reactor, the control valve should be selected as
Afail-open, so that cooling continues if the air supply fails
Bfail-closed, to stop the flow of water
Cfail-in-place
Deither, since it makes no difference
Answer is hidden
Question 12 of 78Introduction to Process Control, Modelling and Controller Modes
An equal percentage valve characteristic means that
Athe flow is independent of stem position
Bthe valve passes most of its flow in the first part of the travel
Cequal increments of lift produce equal increments of flow
Dequal increments of stem lift produce equal percentage changes in the existing flow
Answer is hidden
Question 13 of 78Introduction to Process Control, Modelling and Controller Modes
Cavitation in a control valve occurs when the pressure at the vena contracta falls below the liquid's vapour pressure and
Athe valve is fully closed
Bthe downstream pressure remains below the vapour pressure
Cthe downstream pressure then recovers above the vapour pressure, collapsing the bubbles
Dthe liquid temperature falls sharply
Answer is hidden
Question 14 of 78Advanced Control Schemes
The principal advantage of feedforward control over feedback control is that it
Ais unaffected by model inaccuracy
Bhandles unmeasured disturbances automatically
Ctakes corrective action before the disturbance affects the controlled variable
Drequires no measurement of any kind
Answer is hidden
Question 15 of 78Advanced Control Schemes
The most serious limitation of pure feedforward control is that
Ait responds only after an error appears
Bit always makes the loop unstable
Cit cannot compensate for disturbances that are not measured
Dit cannot be combined with feedback
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Question 16 of 78Advanced Control Schemes
In a cascade control system, the output of the master controller serves as
Athe measurement of the slave controller
Bthe set point of the slave controller
Cthe disturbance to the process
Dthe direct signal to the control valve
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Question 17 of 78Advanced Control Schemes
For cascade control to be effective, the inner (slave) loop must be
Asignificantly slower than the outer loop
Bsignificantly faster than the outer loop, typically by a factor of three to five
Ccontrolled by a PID controller with derivative action
Dexactly the same speed as the outer loop
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Question 18 of 78Advanced Control Schemes
In a cascade control system, integral action is normally required in
Aboth controllers equally
Bneither controller
Cthe slave controller only
Dthe master controller only
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Question 19 of 78Advanced Control Schemes
In ratio control, the stream that is measured but not manipulated is called the
Acontrolled stream
Bmanipulated stream
Cset point stream
Dwild stream
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Question 20 of 78Advanced Control Schemes
The preferred implementation of ratio control multiplies the measured wild flow by the desired ratio rather than dividing two measurements because
Athe ratio would otherwise be inverted
Bdivision amplifies measurement noise at low flow rates
Cdivision cannot be performed by a controller
Dmultiplication is cheaper to implement
Answer is hidden
Question 21 of 78Advanced Control Schemes
Split-range control refers to an arrangement in which
Athe signal is split between the controller and the recorder
Bone controller output drives two or more final control elements over different parts of its range
Cthe control range is divided between two operators
Dtwo controllers share one measurement
Answer is hidden
Question 22 of 78Advanced Control Schemes
Tray temperature is commonly used to control composition in a distillation column because
Atemperature is the variable to be controlled
Bcomposition is not important in distillation
Con-line composition analysers are slow and expensive, and temperature responds quickly
Dtemperature is unaffected by pressure changes
Answer is hidden
Question 23 of 78Advanced Control Schemes
Pressure control is established first on a distillation column because
Apressure affects only the condenser
Brelative volatility, and hence the entire separation, depends on pressure
Cpressure is the easiest variable to measure
Dthe column cannot be started otherwise
Answer is hidden
Question 24 of 78Advanced Control Schemes
In the relative gain array, a relative gain of exactly 1.0 for a particular pairing indicates that
Athe loop is unstable
Bthe loop does not interact with the other loops
Cthe pairing must be avoided
Dthe loops interact very strongly
Answer is hidden
Question 25 of 78Advanced Control Schemes
A pairing with a negative relative gain should
Abe used only with derivative action
Bnever be used, because the loop will be unstable if the other loop is switched off or saturates
Cbe used only for level loops
Dalways be preferred, since it shows strong coupling
Answer is hidden
Question 26 of 78Advanced Control Schemes
Cascade control of reactor temperature onto jacket temperature is used because
Ait removes the need for integral action anywhere
Bit eliminates the need for a control valve
Cdisturbances in the coolant supply are corrected by the fast inner loop before they reach the reactor
Dthe jacket temperature is the variable of real interest
Answer is hidden
Question 27 of 78Linear Open-loop Systems
A first-order system subjected to a step input reaches what percentage of its final value in one time constant?
A95 per cent
B50 per cent
C86.5 per cent
D63.2 per cent
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Question 28 of 78Linear Open-loop Systems
A first-order system responding to a step change
Aoscillates with decaying amplitude
Bapproaches its final value exponentially without overshoot or oscillation
Covershoots and then settles
Dresponds instantaneously
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Question 29 of 78Linear Open-loop Systems
A liquid level tank whose outflow is maintained by a constant-displacement pump behaves as
Aa second-order underdamped system
Ba first-order system with time constant AR
Ca pure integrator with no self-regulation
Da system with dead time only
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Question 30 of 78Linear Open-loop Systems
A second-order system with a damping coefficient of 0.5 will
Aapproach the final value without any overshoot
Boscillate with decaying amplitude and overshoot its final value
Coscillate with constant amplitude
Ddiverge from the final value
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Question 31 of 78Linear Open-loop Systems
The fastest response of a second-order system that exhibits no overshoot at all occurs when the system is
Aoverdamped, with ΞΆ greater than 1
Bundamped, with ΞΆ = 0
Cunderdamped, with ΞΆ less than 1
Dcritically damped, with ΞΆ = 1
Answer is hidden
Question 32 of 78Linear Open-loop Systems
The decay ratio of an underdamped second-order response is related to the overshoot by
Adecay ratio = overshoot
Bdecay ratio = (overshoot)Β²
Cdecay ratio = βovershoot
Ddecay ratio = 1 β overshoot
Answer is hidden
Question 33 of 78Linear Open-loop Systems
Two non-interacting first-order systems in series will produce a response that is
Aalways overdamped and therefore never oscillatory
Bunstable
Calways underdamped and oscillatory
Dcritically damped in every case
Answer is hidden
Question 34 of 78Linear Open-loop Systems
A U-tube manometer is a classic example of a second-order system because it possesses
Atwo non-interacting capacities
Binertia of the liquid column, a gravitational restoring force and viscous damping
Ca pure integrating action
Ddead time and a first-order lag
Answer is hidden
Question 35 of 78Linear Open-loop Systems
Compared with the corresponding non-interacting system, two interacting tanks in series give a response that is
Aidentical in every respect
Bfaster, because the tanks assist each other
Coscillatory
Dmore sluggish, because interaction increases the effective damping
Answer is hidden
Question 36 of 78Linear Open-loop Systems
The transfer function representing a dead time of ΞΈ is
AΞΈs
B1/ΞΈs
C1/(ΞΈs + 1)
DeβΞΈs
Answer is hidden
Question 37 of 78Linear Open-loop Systems
Dead time is particularly troublesome in a feedback control loop because it
Areduces the process gain to zero
Beliminates the steady-state offset
Cincreases the amplitude ratio at high frequency
Dadds phase lag that grows without limit as frequency rises, while causing no attenuation
Answer is hidden
Question 38 of 78Linear Open-loop Systems
A process with a large ratio of dead time to time constant is best handled by
Aincreasing the controller gain sharply
Bdetuning the controller or using a dead-time compensator such as a Smith predictor
Cadding more derivative action
Dremoving integral action entirely
Answer is hidden
Question 39 of 78Linear Open-loop Systems
Inverse response, in which the output initially moves in the direction opposite to its eventual change, is caused by
Aexcessive integral action
Ba pole at the origin
Ca zero in the right half of the complex plane
Da negative steady-state gain
Answer is hidden
Question 40 of 78Linear Closed-loop Systems
For a simple feedback loop, the closed-loop transfer function for a set point change is
Athe inverse of the open-loop transfer function
Bthe product of the forward path blocks divided by one plus the open-loop transfer function
Cthe product of all blocks around the loop
Done plus the open-loop transfer function
Answer is hidden
Question 41 of 78Linear Closed-loop Systems
When a first-order process is placed under proportional control, the closed-loop time constant is
Azero
Bidentical to that of the process
Clarger than that of the process alone
Dsmaller than that of the process alone, so the response is faster
Answer is hidden
Question 42 of 78Linear Closed-loop Systems
For a first-order process under proportional control with loop gain product KcKp, the offset following a unit step change in set point is
Azero
BKcKp/(1 + KcKp)
C1/(1 + KcKp)
D1 + KcKp
Answer is hidden
Question 43 of 78Linear Closed-loop Systems
Adding integral action to a proportional controller on a first-order process
Aleaves the closed-loop order unchanged
Braises the order of the closed loop to two and can cause overshoot
Cguarantees that the response cannot oscillate
Dmakes the closed loop first order
Answer is hidden
Question 44 of 78Linear Closed-loop Systems
The characteristic equation of a feedback control system is
A1 + GOL = 0
BGOL = 0
C1 β GOL = 0
DGOL = 1
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Question 45 of 78Linear Closed-loop Systems
A feedback control system is stable if and only if
Aat least one root has a negative real part
Ball roots are real
Cthe open-loop gain is greater than one
Dall roots of the characteristic equation have negative real parts
Answer is hidden
Question 46 of 78Linear Closed-loop Systems
If one coefficient of the characteristic polynomial is negative while the others are positive, the system is
Acertainly stable
Bstable only if the gain is low
Cmarginally stable
Dcertainly unstable
Answer is hidden
Question 47 of 78Linear Closed-loop Systems
In the Routh array, the number of roots lying in the right half of the complex plane equals
Athe degree of the polynomial
Bthe number of rows in the array
Cthe number of zero entries in the array
Dthe number of sign changes in the first column
Answer is hidden
Question 48 of 78Linear Closed-loop Systems
The ultimate gain of a control loop is the proportional gain at which
Athe offset becomes zero
Bthe loop oscillates continuously with constant amplitude
Cthe response becomes critically damped
Dthe controller output saturates
Answer is hidden
Question 49 of 78Linear Closed-loop Systems
Which of the following changes tends to make a control loop less stable?
ARemoving a lag from the loop
BAdding derivative action
CDecreasing the controller gain
DIncreasing the dead time in the loop
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Question 50 of 78Linear Closed-loop Systems
A first-order process controlled by a purely proportional controller is
Astable for any value of the controller gain
Balways unstable
Cstable only at very low gain
Dunstable above a certain gain
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Question 51 of 78Linear Closed-loop Systems
The standard electronic instrument signal range is
A0 to 20 mA
B3 to 15 mA
C0 to 10 V only
D4 to 20 mA
Answer is hidden
Question 52 of 78Linear Closed-loop Systems
Persistent cycling of an otherwise well-tuned control loop is most commonly caused by
Aexcessive derivative gain
Btoo wide a proportional band
Cstiction in the control valve stem packing
Dan oversized transmitter span
Answer is hidden
Question 53 of 78Frequency Response and Controller Tuning
When a stable linear system is subjected to a sustained sinusoidal input, the output is
Aa sinusoid of the same frequency but different amplitude and phase
Ba steady constant value
Ca sinusoid of different frequency
Dan exponentially growing signal
Answer is hidden
Question 54 of 78Frequency Response and Controller Tuning
For a first-order lag at the corner frequency, the amplitude ratio and phase angle are
A0.707 and β90Β°
B1.0 and 0Β°
C0.707 and β45Β°
D0.5 and β90Β°
Answer is hidden
Question 55 of 78Frequency Response and Controller Tuning
The high-frequency asymptote of the Bode amplitude plot for a first-order lag has a slope of
Aβ40 decibels per decade
Bzero
Cβ20 decibels per decade
Dβ10 decibels per decade
Answer is hidden
Question 56 of 78Frequency Response and Controller Tuning
The amplitude ratio of a pure dead time element is
Aproportional to frequency
Bunity at all frequencies
Cinversely proportional to frequency
Dzero at all frequencies
Answer is hidden
Question 57 of 78Frequency Response and Controller Tuning
According to the Bode stability criterion, a closed-loop system is stable if the open-loop amplitude ratio is
Aequal to 1 at zero frequency
Bless than 1 at all frequencies
Cgreater than 1 at the frequency where the phase lag is β180Β°
Dless than 1 at the frequency where the phase lag is β180Β°
Answer is hidden
Question 58 of 78Frequency Response and Controller Tuning
The phase angle contributed by a pure integrating element is
Aβ90Β° at all frequencies
Bβ45Β° at all frequencies
C0Β°
D+90Β° at all frequencies
Answer is hidden
Question 59 of 78Frequency Response and Controller Tuning
The gain margin of a control loop is defined as
Athe ultimate gain divided by the actual gain at all frequencies
Bthe reciprocal of the open-loop amplitude ratio at the crossover frequency
C180Β° plus the phase angle where AR = 1
Dthe amplitude ratio at zero frequency
Answer is hidden
Question 60 of 78Frequency Response and Controller Tuning
A recommended design value for the phase margin of a control loop is
A90 to 120 degrees
B180 degrees
C30 to 45 degrees
D0 to 5 degrees
Answer is hidden
Question 61 of 78Frequency Response and Controller Tuning
In the Ziegler-Nichols continuous cycling method, the controller gain for a PI controller is set at
A0.6 Kcu
B1.2 Kcu
C0.5 Kcu
D0.45 Kcu
Answer is hidden
Question 62 of 78Frequency Response and Controller Tuning
The principal practical objection to the Ziegler-Nichols continuous cycling tuning method is that
Ait cannot be used on PI controllers
Bit requires the plant to be driven to the point of sustained oscillation
Cit needs a mathematical model of the process
Dit gives an excessively sluggish response
Answer is hidden
Question 63 of 78Frequency Response and Controller Tuning
The process reaction curve method of tuning requires
Ano plant test at all
Bdriving the loop to continuous oscillation
Ca single step test with the controller in manual
Da frequency response test over many frequencies
Answer is hidden
Question 64 of 78Frequency Response and Controller Tuning
Among the integral error criteria, the one that gives the least oscillatory controller settings is
AIAE
BISE
Call three give identical settings
DITAE
Answer is hidden
Question 65 of 78Frequency Response and Controller Tuning
A control loop that cycles slowly and continuously, and whose behaviour does not improve at any controller setting, most probably suffers from
Atoo high a controller gain
Btoo much derivative action
Cstiction or hysteresis in the control valve
Dan incorrectly ranged transmitter
Answer is hidden
Question 66 of 78Instrumentation
The accuracy of an instrument refers to
Ahow close its reading is to the true value
Bthe slope of its calibration curve
Chow closely repeated readings agree with one another
Dthe smallest change it can detect
Answer is hidden
Question 67 of 78Instrumentation
A thermocouple generates an EMF as a result of
Athe differential expansion of two bonded metals
Bthe Seebeck effect at the junction of two dissimilar metals
Cthe emission of thermal radiation
Dthe change in electrical resistance with temperature
Answer is hidden
Question 68 of 78Instrumentation
Compared with a thermocouple, a platinum resistance thermometer offers
Ano need for any external power supply
Ba faster response and higher output voltage
Cgreater accuracy, stability and linearity but a narrower range and slower response
Da wider temperature range and lower cost
Answer is hidden
Question 69 of 78Instrumentation
A piezoelectric pressure transducer is unsuitable for measuring
Aa steady, unchanging pressure
Bvibration
Crapidly fluctuating pressures
Dshock and blast pressures
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Question 70 of 78Instrumentation
An electromagnetic flowmeter can be used only when the fluid
Acontains no suspended solids
Bis non-conductive
Cis electrically conductive
Dis a gas
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Question 71 of 78Instrumentation
The instrument that measures true mass flow rate directly, rather than inferring it from volumetric flow, is the
Aorifice meter
Bvortex shedding meter
CCoriolis meter
Dturbine meter
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Question 72 of 78Instrumentation
Differential pressure measurement of liquid level requires that
Athe liquid be electrically conductive
Bthe density of the liquid be known and reasonably constant
Cthe tank be open to the atmosphere
Dthe liquid contain no solids
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Question 73 of 78Instrumentation
The Karl Fischer titration is used specifically for the determination of
Adissolved oxygen
Bwater content
Ctotal solids content
DpH
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Question 74 of 78Instrumentation
At 25 Β°C, the theoretical response of a glass pH electrode is approximately
A1.0 mV per pH unit
B59.16 mV per pH unit
C100 mV per pH unit
D0.059 mV per pH unit
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Question 75 of 78Instrumentation
The glass membrane of a pH electrode must never be allowed to dry out because
Athe cable will become disconnected
Bthe reference electrolyte will crystallise
Cthe hydrated gel layer responsible for the response is lost and the electrode fails
Dthe glass will crack immediately
Answer is hidden
Question 76 of 78Instrumentation
pH control is regarded as one of the most difficult control problems because
Athe titration curve is extremely non-linear, so the process gain varies by orders of magnitude
BpH responds too slowly to be controlled
Creagent valves cannot be automated
DpH cannot be measured on line
Answer is hidden
Question 77 of 78Instrumentation
In reversed phase HPLC, the stationary phase is non-polar and the mobile phase polar, so
Aelution order depends only on molecular weight
Ball compounds elute at the same time
Cpolar compounds elute first and non-polar compounds are retained longest
Dnon-polar compounds elute first
Answer is hidden
Question 78 of 78Instrumentation
HPLC is preferred to gas chromatography for the analysis of
Apermanent gases
Bvolatile solvents only
Cnon-volatile and thermally labile compounds such as proteins and many pharmaceuticals
Dlight hydrocarbons
Answer is hidden