Objective:
By the end of this module, a trainee will be able to:
Understand basic instrumentation types used in petrochemical plants.
Recognize common control loops and their purposes.
Understand operator interaction with DCS (Distributed Control System) or PLC (Programmable Logic Controller).
Monitor alarms, trends, and process variables effectively.
Apply basic troubleshooting for instrumentation and control issues.
Definition:
Instrumentation = devices that measure, monitor, and transmit process variables such as temperature, pressure, flow, and level.
Control Systems = automated systems that regulate process variables to maintain desired operating conditions.
Importance:
Ensures process stability, safety, and product quality.
Allows operators to monitor processes remotely.
Provides alarms and interlocks to prevent abnormal conditions.
Operator Role:
Monitor readings, trends, and alarms on control panels.
Respond to abnormal signals or equipment status.
Communicate with maintenance if instruments show abnormal behavior.
Analogy:
Instrumentation = “sensors on a car (speedometer, fuel gauge, temperature gauge).”
Control system = “cruise control maintaining speed automatically.”
Temperature Transmitter (TT)
Measures process temperature
Monitor trends, check calibration if readings abnormal
Pressure Transmitter (PT)
Measures pressure
Verify against gauges, alarm on deviation
Flow Meter (FT)
Measures liquid or gas flow
Ensure flow within process limits
Level Transmitter (LT)
Measures liquid level in tanks/columns
Monitor high/low alarms, maintain level control
Valve Positioner (PV)
Shows valve opening
Ensure valve responds to control signal
Gas Detector
Detects toxic/flammable gases
Respond to alarm, ensure safety
pH/Conductivity Sensor
Measures chemical properties
Monitor trends, prevent off-spec product
Operator Tips:
Regularly check sensor readings vs expected values.
Report abnormal trends, faulty instruments, or alarms.
Never adjust calibration unless trained and authorized.
Definition:
Control Loop = a system that measures a process variable and adjusts output to maintain setpoint.
Types of Loops:
ON/OFF Control – simplest, turns equipment fully on or off based on setpoint.
PID Control (Proportional-Integral-Derivative) – continuously adjusts output to maintain setpoint.
Cascade Control – one loop controls another loop for more precise control.
Feedforward Control – anticipates changes based on measured disturbances.
Operator Role:
Monitor setpoints, control response, and loop performance.
Detect loop oscillations, slow response, or saturation.
Notify maintenance if control issues persist.
Analogy:
PID control = “thermostat adjusting heater output to maintain room temperature.”
DCS (Distributed Control System):
Centralized monitoring with operator stations, controllers, and field devices.
Ideal for continuous processes like butadiene plants.
PLC (Programmable Logic Controller):
Focused on discrete control of equipment like pumps, compressors, and valves.
Operator Role:
Observe process variables and alarms on screens.
Execute manual actions if automated systems cannot resolve abnormal conditions.
Follow SOPs for start/stop, interlock override, or ESD activation.
Analogy:
DCS = “central dashboard of a city traffic control system.”
PLC = “traffic light controller at a single intersection.”
Definition:
Alarm = alert indicating process variable is outside normal range.
Types of Alarms:
High/Low Process Variable – e.g., temperature, pressure, level.
Equipment Status – pump failure, compressor trip.
Safety/ESD Alarm – fire, gas, or critical overpressure.
Operator Role:
Acknowledge alarms according to SOP.
Investigate cause promptly.
Take corrective action or notify maintenance.
Avoid ignoring recurring alarms (“alarm fatigue”).
Sensor reading stuck
Faulty transmitter, broken wiring
Verify with backup instrument, notify maintenance
Alarm triggered but process normal
Sensor calibration drift, false alarm
Confirm with secondary measurement, report
Valve not responding
Actuator issue, control signal lost
Check manual operation, verify control signal, notify maintenance
Flow reading zero
Blocked line, sensor fault
Inspect line, compare with other measurements, notify maintenance
Operator Tips:
Always cross-check with secondary instruments or visual inspection.
Never bypass alarms without proper authorization.
Document all troubleshooting actions.
Name four common types of process instrumentation.
What is a PID control loop and why is it important?
How does an operator respond to a high-pressure alarm?
What is the difference between DCS and PLC?
Why is alarm management important?
Give an analogy for instrumentation and control systems.
Videos:
Operator interaction with DCS/PLC
Control loop demonstration (ON/OFF, PID)
Alarm response simulation
Diagrams / Infographics:
Process instrumentation layout
Control loop schematic
Alarm priority flowchart
PDF Downloads:
Instrumentation checklist
Control loop monitoring guide
Alarm response guide
Interactive:
Embedded quizzes
Scenario exercises: detect abnormal variable and take action
Instrumentation measures key process variables; control systems maintain setpoints.
Operators monitor DCS/PLC, alarms, and trends continuously.
Control loops (ON/OFF, PID, cascade, feedforward) regulate process performance.
Alarm management ensures timely response to abnormal conditions.
Troubleshooting instrumentation requires cross-checking readings, following SOPs, and communication with maintenance.