Why Ratio Control System Caused Reactor Temperature Fluctuation?

Why Ratio Control System Caused Reactor Temperature Fluctuation?

A chemical plant used a ratio control system to maintain the correct proportion between reactant A and catalyst flow entering a reactor. The process normally operated with a fixed 5:1 ratio to maintain stable reaction temperature and product quality. During a production increase, operators noticed sudden reactor temperature fluctuations, off specification product quality, and continuous oscillation in the catalyst control valve.

The main reactant flow was considered the wild flow and frequently changed according to production demand. The catalyst flow control loop automatically adjusted itself to maintain the required ratio. However, after the throughput increased rapidly, the catalyst valve started hunting continuously and the reactor temperature became unstable.

Field technicians checked the control valve, flow transmitter calibration, and reactor temperature sensor, but all instruments were functioning normally. Trending analysis later showed that the catalyst flow controller was responding too aggressively to rapid changes in the wild flow signal. The PID tuning of the secondary ratio loop had high proportional gain and integral action, causing overshoot whenever the primary flow changed suddenly.

Engineers modified the PID tuning, added signal filtering to the wild flow measurement, and limited the rate of change for the catalyst flow setpoint. After implementing these corrections, the ratio stabilized and the reactor temperature returned to normal operating conditions.

The ratio control system became unstable because the secondary flow controller reacted too aggressively to sudden variations in the primary wild flow. In ratio control systems, one process variable changes freely while the second variable automatically follows it according to a predefined ratio. If the primary flow changes too quickly, the secondary controller may continuously chase the changing setpoint, causing oscillation and unstable control behavior.

This problem commonly occurs in process industries when PID tuning is too aggressive or when rapid flow disturbances are introduced during production changes. High proportional gain and excessive integral action can create valve hunting, overshoot, and reactor instability. In severe cases, incorrect ratio response may affect chemical reaction efficiency, combustion stability, or blending accuracy.

Signal filtering, proper cascade tuning, controlled setpoint ramping, and stable flow measurement are important for maintaining reliable ratio control performance. Engineers must also verify control valve response time and transmitter stability during commissioning and process load changes.

Refer the below link for ratio control system basics