AUS-ETO-L3.1

Automation and control systems — PLCs, loops and tuning

Almost nothing aboard a modern vessel is operated directly any more. A pump does not start because someone pressed a button; it starts because a controller compared a measured value with a setpoint and decided it should. Between the operator and the machinery there is now a layer of logic, and that layer is the ETO's.

Entry & progression

Automation does not remove the engineer. It removes the engineer's eyes. The plant now tells you what it thinks is happening. The ETO is the person who can tell whether it is right.

The control loop

  1. A sensor measures the process variable — temperature, pressure, level, speed
  2. A transmitter converts it to a signal the controller understands
  3. A controller compares it with the setpoint and computes an output
  4. A final control element acts — a valve, a drive, a contactor
  5. The process responds, and the sensor measures the result. The loop closes.

Every fault in a loop is in one of those five places, plus the wiring between them. That is a very short list, and it is why loop faults should never be a mystery. The discipline is to establish which element lied, not to guess which one to replace.

PID, honestly

Term Acts on Too much gives you
Proportional The present error Oscillation, hunting
Integral The accumulated error over time Slow overshoot; wind-up after a saturation
Derivative The rate of change of error Amplified noise; twitchy output

Proportional alone leaves a standing offset — the loop settles near the setpoint, not on it. Integral removes the offset but adds lag. Derivative anticipates, and faithfully amplifies every bit of electrical noise on the signal. Most marine loops are PI. Derivative is used sparingly and on clean signals.

TIP — Before you tune, check the loop is not lying to you A large proportion of 'tuning problems' are instrument problems. A sticking valve, a fouled sensor, a transmitter drifting out of calibration, a loose terminal — all of these look exactly like a badly tuned loop from the screen.

Confirm the measurement is true and the final element actually moves where it is told. Then touch the gains. Tuning around a mechanical fault produces a loop that is broken in two ways.

PLCs and where they hide

Programmable logic controllers run the sequences: engine safety and start logic, fuel and lube transfer, bilge and ballast, HVAC plant, fire dampers, thruster and stabiliser permissives. A PLC scans its inputs, executes its program, and writes its outputs — thousands of times a minute, identically, forever.

It is a machine that does exactly what it was told. When a system 'behaves strangely', the PLC is almost never wrong; the input it is reading is wrong, the interlock it is honouring is one you have forgotten, or the logic was written for a plant that has since been modified.

NOTE — Software is a maintained item Programs, setpoints and drive parameters are part of the plant, and they are the part with no spare in the store. Keep a current backup of every PLC program and every drive parameter set, keep it off the vessel as well as on it, and record every change — what, when, why, by whom.

A controller that fails on a Sunday with no backup is not an electrical fault. It is a project.

Practice questions

5 questions
recallcore

recall · core

A fault in a closed control loop must lie in one of: (a) The setpoint or the operator (b) The controller software only (c) The power supply or the network (d) The sensor, transmitter, controller, final control element, process — or the wiring between them

recallcore

recall · core

Proportional control acting alone characteristically leaves: (a) A standing offset from the setpoint (b) Integral wind-up (c) Amplified signal noise (d) Zero steady-state error

recallcore

recall · core

Derivative action is used sparingly in marine loops because it: (a) Cannot remove steady-state error (b) Requires a faster processor (c) Amplifies noise on the measured signal (d) Is prohibited by class rules

recallcore

recall · core

Before adjusting PID gains on a badly behaving loop, you should first: (a) Increase the integral time (b) Switch the loop to manual and leave it there (c) Reduce the setpoint (d) Confirm the measurement is true and the final control element actually moves as commanded

recallcore

recall · core

PLC programs and drive parameter sets should be treated as: (a) Vendor property, not to be recorded aboard (b) Maintained items — backed up, held off the vessel as well as on it, and change-logged (c) Fixed at commissioning and never changed (d) Documentation only, with no operational consequence

AI-drafted catalogue content pending SME review. Sea service and course requirements change; verify with AMSA before relying on this for a career decision.

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