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POC 01Reproducible now

Self-Regulating Process Control Under Sensor Degradation

The control loop that automatically widens its safety margin when instruments degrade — and tightens again when they recover.

±0.3%
SolvSRK max setpoint deviation
±4.7%
Standard PID max overshoot
0
SolvSRK safety trips (100 cycles)
2
Standard PID safety trips (100 cycles)

The scenario

Set the picture

A continuous chemical reactor holds temperature within ±0.5°C of a 185°C setpoint. The control loop reads a bank of four thermocouples, averages them, and drives a steam valve. Over a 6-month campaign, thermocouples drift, foul, and occasionally fail — but the PID gains were tuned on day one and never change.

The same pattern shows up across every process plant: extrusion lines, pharmaceutical reactors, food-processing pasteurizers, paper-mill dryers, semiconductor CVD chambers. Fixed-gain loops running on degrading sensors.

Cost today

Fixed-gain PID under sensor degradation either overshoots into a safety trip (lost batch, 4–8 hours of recovery) or limps at conservative setpoints (2–5% throughput penalty per shift). Both cost money.

Adaptive-gain schemes exist but require a model of the degradation mode, re-tuning on a schedule, and engineering hours per loop per quarter. Plants with 2,000+ loops cannot keep up.

What changes with SolvSRK

SolvSRK tracks state-space uncertainty inside the integration step. When thermocouple readings diverge (one drifting, three stable), the uncertainty envelope widens — and the controller automatically backs off gain, widening the proportional band. When the faulty sensor is replaced, uncertainty tightens and the loop returns to tight control.

Across 5 degradation profiles (drift, noise spike, bias shift, intermittent dropout, correlated double fault), SolvSRK held ±0.3% of setpoint with zero trips. The standard PID exceeded ±4.7% overshoot and tripped twice in 100 challenge cycles.

No re-tuning. No degradation model. No per-loop engineering. The safety margin is live, not designed-in.

Measurable outcome

What we claim — and how it survives review

Each line below maps to a captured number in the demo section. Every number is reproducible from the benchmark suite.

  • ±0.3% setpoint accuracy under all 5 sensor degradation profiles (standard PID: ±4.7%).
  • Zero safety trips across 100 challenge cycles (standard PID: 2 trips).
  • No per-loop tuning or degradation-mode model required.
  • Uncertainty envelope visible to operator — confidence interval on every reading, not just the point estimate.
  • Compatible with existing 4–20 mA / HART / Profibus instrument buses.

The demo

What was tested. How. What the simulation printed.

Simulated continuous reactor with 4 thermocouples, a steam valve, and a 185°C setpoint. 100 challenge cycles across 5 degradation profiles: slow drift (0.1°C/hour), noise spike (±2°C burst), bias shift (+1.5°C step), intermittent dropout (5-second gaps), and correlated double fault (2 of 4 sensors drifting in the same direction).

Two controllers run in parallel on the same plant model: standard industrial PID (Ziegler-Nichols tuned) and SolvSRK self-regulating control. Measured: max overshoot, trip count, time to recover after sensor replacement.

Captured benchmark output

The numbers the simulation actually printed.

Control performance across 5 sensor degradation profiles
ProfileSolvSRK max devPID max devSolvSRK tripsPID trips
Slow drift0.21%2.1%00
Noise spike0.30%4.7%01
Bias shift0.18%3.2%00
Intermittent dropout0.27%3.8%01
Correlated double0.24%4.1%00

Standard PID: Ziegler-Nichols tuned on clean instruments. SolvSRK: single configuration, no per-profile tuning.

Evidence pointers

Where the claims live in the evidence register

These are the validation sources a reviewer should trace to verify every number on this page.

  • SolvSRK self-regulating control validation suite
  • SolvSRK Real-Time UQ — calibrated uncertainty envelopes
  • Robotics vertical — validated claims for self-regulating control
  • SolvSRK dynamics validation — stability under contested noise (91%+ survival)

Want to see these numbers on your plant?

Run the benchmark on your actual process model.

Two weeks, fully credited. No production integration needed. Every claim above traces back to a simulation you can verify.

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