Split Range Pressure Control – Interactive Simulator
One pressure controller drives two valves. When pressure is low the controller opens the gas IN valve to refill the drum. When pressure is high it opens the FLARE valve to vent gas. In the middle both valves stay shut. Create a disturbance, or switch to Manual and drag the controller output to see how the output is split between the two valves.
What is happening now
Readings
| Drum pressure (PV) | |
| Setpoint (SP) | |
| Error (PV – SP) | |
| Controller output (OUT) | |
| Gas IN valve opening | |
| FLARE valve opening | |
| Gas flowing in | |
| Gas going to flare | |
| Process gas imbalance |
Why use split range?
1Mode and setpoint
2Create a disturbance
3Set the split range
4Watch
Split range graph (click it to set OUT)
Pressure trend
Controller output and valves
Split Range Pressure Control – Interactive Simulator
Understand the working principle of split range pressure control through an interactive simulation of a gas surge drum. A single Pressure Indicating Controller (PIC) regulates drum pressure by controlling two valves: a gas inlet valve and a flare valve. When drum pressure falls below the setpoint, the gas inlet valve opens to increase pressure. When pressure rises above the setpoint, the flare valve opens to release excess gas. Within the configured dead band, both valves remain closed.
Experiment with Auto and Manual modes, adjust the pressure setpoint, split point, and dead band, and introduce gas supply disturbances to observe how the system responds. Real-time visual animations, controller output calculations, valve opening indicators, pressure trends, and process flow readings help you understand the relationship between controller output and valve operation.
This simulator is designed for instrumentation engineers, DCS/PLC learners, process control students, and maintenance technicians who want to build practical knowledge of split range control, pressure regulation, and control valve behavior.
Note: This is an educational simulation with simplified process dynamics, not a substitute for actual plant control logic or safety system design.
