HKIE Professional Assessment - Control, Automation & Instrumentation Discipline flashcards
HKIE Professional Assessment - Control, Automation & Instrumentation Discipline · Build recall with a focused review session.
32 cards. Read the term and the definition here. The deck at the top of this page is optional.
- PID parallel form
- The ideal PID controller in parallel form is u(t) = Kp e(t) + Ki ∫e dt + Kd de/dt, where Ki and Kd are independent gains and the Laplace form is C(s) = Kp + Ki/s + Kd s.
- Routh-Hurwitz stability criterion
- A necessary condition for stability is that all coefficients of the characteristic polynomial are positive. A sufficient condition is that the first column of the Routh array has no sign changes.
- Gain margin and phase margin
- Gain margin is the negative of the gain in dB at the phase crossover where phase equals −180°. Phase margin is 180° plus the phase at the gain crossover where gain is 0 dB.
- Ziegler-Nichols ultimate gain tuning
- With proportional-only control at the ultimate gain Ku and ultimate period Pu, PID settings are Kp = 0.6Ku, Ti = 0.5Pu, and Td = 0.125Pu. Use with caution on dead-time-dominant processes.
- 4–20 mA live zero
- In a 4–20 mA loop, 4 mA represents 0% and 20 mA represents 100%. The live zero allows detection of a broken wire, which reads 0 mA and is distinguishable from a valid zero signal.
- Maximum loop resistance
- For a 4–20 mA loop, R_max = (Vsupply − Vmin_transmitter)/0.020 A. With a 24 V supply and 12 V minimum transmitter voltage, the maximum loop resistance is 600 Ω.
- Orifice plate square-root relationship
- Differential pressure across an orifice is proportional to the square of flow: Q ∝ √ΔP. The transmitter signal must be square-root extracted to obtain a linear flow indication.
- Intrinsic safety entity parameters
- Intrinsically safe circuits are verified by matching entity parameters: the barrier output voltage Uo, current Io, capacitance Co, and inductance Lo must not exceed the hazardous-area device ratings Ui, Ii, Ci, and Li.
- PLC scan cycle
- A PLC repeats: read inputs, execute the program, update outputs, then perform housekeeping and communications. Worst-case response time includes at least one full scan plus input filter delay.
- Seal-in circuit
- A seal-in or latching circuit places a normally-open contact in parallel with the start pushbutton so that the output remains energised after the button is released, until a stop or fault contact opens.
- Bumpless transfer
- Bumpless transfer ensures that when a controller switches between manual and automatic, the output does not jump. The integral term is initialised to the current output to prevent a step change.
- ISA-18.2 alarm rationalisation
- ISA-18.2 requires each alarm to be actionable, prioritised, and rationalised. A common target is fewer than six alarms per operator per hour and fewer than 150 alarms per day in steady state.
- OPC UA security
- OPC UA provides platform-independent data exchange with built-in authentication, signing, and encryption. Unlike classic OPC DA, it does not rely on DCOM, which is difficult to secure across networks.
- Time synchronisation for sequence of events
- Accurate time synchronisation using NTP or IEEE 1588 PTP is required so that alarms and trips recorded on different devices can be ordered correctly in a sequence-of-events analysis.
- SIL PFDavg ranges
- In low-demand mode, SIL 1 corresponds to PFDavg between 10⁻¹ and 10⁻², SIL 2 between 10⁻² and 10⁻³, SIL 3 between 10⁻³ and 10⁻⁴, and SIL 4 between 10⁻⁴ and 10⁻⁵.
- Proof test interval effect
- For a simplex element, PFDavg ≈ λDU·T/2, where T is the proof-test interval. Doubling the proof-test interval approximately doubles the average probability of failure on demand.
- Common-cause failure beta factor
- Redundant identical devices are not fully independent. The beta factor models the fraction of failures that are common cause; diversity, physical separation, and different technologies reduce beta.
- SIS independence from BPCS
- A safety instrumented function must be independent of the basic process control system. Sharing sensors or final elements between control and safety requires justification through risk assessment.
- PROFIBUS DP segment rules
- A PROFIBUS DP segment supports up to 32 devices without a repeater, requires 120 Ω termination at both physical ends, and reaches 1200 m at 93.75 kbit/s, with shorter distances at higher speeds.
- HART digital signal
- HART superimposes a frequency-shift-keyed digital signal of about ±0.5 mA at 1200 baud on the 4–20 mA analogue loop, allowing configuration and diagnostics without interrupting the process signal.
- IEC 62443 zones and conduits
- IEC 62443 segments an industrial control system into zones of similar security requirements, connected by conduits that enforce and monitor traffic. This limits lateral movement of an attacker.
- Valve flow coefficient Cv
- Cv is the number of US gallons per minute of water at 60 °F that flows through a valve with a pressure drop of 1 psi. The metric equivalent is Kv, where Kv = 0.865 Cv.
- Equal percentage valve characteristic
- In an equal percentage valve, equal increments of stem travel produce equal percentage changes in flow. It is often chosen because the installed characteristic becomes approximately linear.
- Cavitation versus flashing
- Cavitation occurs when the vena contracta pressure falls below vapour pressure and bubbles collapse downstream. Flashing occurs when downstream pressure remains below vapour pressure and bubbles persist.
- Fail-safe valve action
- Spring-return actuators provide fail-safe action: air-to-open valves fail closed on loss of air, and air-to-close valves fail open. The choice is a safety decision based on the process hazard.
- BACnet MS/TP
- BACnet MS/TP is a master-slave/token-passing protocol over RS-485 at speeds from 9.6 to 76.8 kbit/s. It is widely used for field devices in building automation systems.
- Economiser free cooling
- An air-side economiser uses outdoor air for cooling when its enthalpy or temperature is below the return air condition, reducing mechanical cooling energy while maintaining supply air setpoint.
- CO₂ demand-controlled ventilation
- Demand-controlled ventilation modulates outdoor air based on measured CO₂ concentration, often targeting 800–1000 ppm, to maintain indoor air quality while reducing fan and conditioning energy.
- Cause-and-effect matrix
- A cause-and-effect matrix cross-references trips, alarms, and outputs to define the required response of the safety and control systems. It is the basis for SIS testing and commissioning.
- Factory acceptance test
- A factory acceptance test verifies the control system against its specification before shipment, including I/O checks, graphics, logic, and interfaces. It reduces site rework and schedule risk.
- Earned value indices
- Cost performance index CPI = EV/AC and schedule performance index SPI = EV/PV. Values below 1.0 indicate cost overrun or schedule slippage relative to the plan.
- IEC 61511 scope
- IEC 61511 is the functional safety standard for safety instrumented systems in the process industry. It covers the safety lifecycle from hazard assessment through design, operation, and decommissioning.