PITOPS
Closed-loop PID tuning software that identifies process models from normal operating data, so loops on crackers, columns, and diagonal-matrix control schemes can be retuned without step tests that disturb production.
Process control software for petrochemical plants optimizes PID tuning, DCS-based advanced process control, multivariable MPC, and control loop monitoring across olefins crackers, aromatics units, and polymer reactors. Each unit interacts differently, from strongly coupled multivariable processes to grade-transition sequences, so it needs a control strategy matched to that interaction pattern rather than one product applied everywhere.
PiControl Solutions selects the control approach based on how a unit actually interacts: full multivariable MPC where variables are strongly coupled, DCS-resident APC built on accurately identified models where the control matrix is diagonal, rather than defaulting to the most complex option available.
It finds underperforming primary and advanced control loops and retunes them against real operating data, without step tests that disturb production or off-spec product.
It keeps process and MPC models accurate as feedstock, catalyst, and market-driven grade targets shift, so the control assets already in the plant deliver the performance they were specified for.
Petrochemical control loops face conditions that generic tuning rarely handles well, because feedstock cost, product demand, and reaction non-linearity shift constantly. PID controllers account for over 95% of all control loops in industrial plants, so tightening these loops and matching the right advanced control approach to each unit is where petrochemical variability is won or lost.
Where a unit is truly multivariable, several manipulated variables couple strongly to several controlled variables, so a single-loop fix in isolation just moves the disturbance somewhere else on the unit.
Product grade transitions require a coordinated sequence of setpoint changes across multiple loops, and a poorly sequenced transition extends off-spec time and wastes both feedstock and reactor time.
Petrochemical economics move constantly as feedstock composition, chemical prices, and customer demand shift, so the optimal operating point for a given unit today is rarely the optimal point next week.
Equipment and process non-linearity, driven by catalyst aging and shifts in raw material properties, means a controller tuned for one operating condition can run stiff or oscillatory once conditions drift.
Three PiControl products carry most petrochemical optimization work, and each targets a different stage of the control problem.
Closed-loop PID tuning software that identifies process models from normal operating data, so loops on crackers, columns, and diagonal-matrix control schemes can be retuned without step tests that disturb production.
Handles closed-loop MPC model identification, refreshing the multivariable models behind olefins and aromatics advanced controllers as feedstock composition and catalyst conditions drift.
Provides continuous control loop monitoring, flagging oscillation, valve stiction, and degrading APC performance across the plant before a grade transition or feedstock swing turns into off-spec product.
Compatible with every major DCS and PLC via OPC-DA and OPC-UA, these products read live data from the control assets, analyzers, and LIMS already installed, so no new control hardware is needed. They form the petrochemical slice of PiControl's process control software range.
Process optimization software depends on two things in petrochemicals: experienced engineers who know when MPC is warranted and when it isn't, and plant teams who can sustain the gains.
PiControl's PID tuning consulting deploys PITOPS and SUPERTUNE directly on petrochemical loops, typically covers 50 to 500 loops per engagement, and documents before-and-after results.
To see how the same optimization layer applies in other sectors, explore process control software by industry.