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arxiv: 2604.12863 · v1 · submitted 2026-04-14 · 📡 eess.SY · cs.SY

Adaptive Tuning of Online Feedback Optimization for Process Control Applications

Pith reviewed 2026-05-10 14:43 UTC · model grok-4.3

classification 📡 eess.SY cs.SY
keywords optimizationtuningadaptivefeedbackonlinecontrolparametersprocess
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The pith

An adaptive tuning scheme for Online Feedback Optimization controllers based on scaled projected gradient descent and objective sensitivity improves closed-loop performance on gas lift and CSTR processes compared to manual tuning.

A machine-rendered reading of the paper's core claim, the machinery that carries it, and where it could break.

Online Feedback Optimization creates controllers by embedding an optimization algorithm inside a feedback loop. This is useful for processes where you lack a complete mathematical model. The difficulty is choosing the right parameters for the optimizer because they do not map directly to physical quantities and their effects are hard to predict. The authors propose making the tuning automatic by measuring how sensitive the performance objective is to changes in those parameters. They focus on scaled projected gradient descent and reduce the operator's choices to two simple numbers: one that sets the maximum allowed change in the control inputs from one step to the next, and one that sets the maximum allowed change in the objective value. These scalars replace the usual collection of hard-to-set algorithm parameters. No extra system information or repeated experiments are required. The method is tested in simulation on a gas-lift oil-production system and on a continuously stirred tank reactor. In both cases the adaptive version produces better closed-loop behavior than the same controller with parameters chosen by hand. The core idea is to let the controller observe its own sensitivity and adjust its internal step sizes on the fly.

Core claim

Numerical studies on a gas lift and a continuously-stirred tank reactor processes confirm that our adaptive scheme improves closed-loop performance of Online Feedback optimization compared to standard manual tuning methods.

Load-bearing premise

The proposed adaptive tuning method limits the operator-tunable parameters to scalar values that represent how much the control inputs and the objective can change between iterations without requiring either additional information about the controlled system or repeated experiments.

read the original abstract

Online Feedback Optimization leverages properties of optimization algorithms to develop controllers for systems with limited model availability, which is often the case in process control. The interplay between the parameters of the chosen optimization algorithm, as well as lack of direct connection to the characteristics of the underlying process make their tuning challenging. We propose a method for adaptive tuning of Online Feedback Optimization controllers based on scaled projected gradient descent by using sensitivity of the desired objective to the parameters of the algorithm. The proposed adaptive tuning method limits the operator-tunable parameters to scalar values that represent how much the control inputs and the objective can change between iterations without requiring either additional information about the controlled system or repeated experiments. Numerical studies on a gas lift and a continuously-stirred tank reactor processes confirm that our adaptive scheme improves closed-loop performance of Online Feedback optimization compared to standard manual tuning methods.

Editorial analysis

A structured set of objections, weighed in public.

Desk editor's note, referee report, simulated authors' rebuttal, and a circularity audit. Tearing a paper down is the easy half of reading it; the pith above is the substance, this is the friction.

Axiom & Free-Parameter Ledger

2 free parameters · 0 axioms · 0 invented entities

The central claim rests on the existence of computable sensitivity of the objective to algorithm parameters and on the assumption that two user scalars suffice to capture allowable changes; no further free parameters or invented entities are described in the abstract.

free parameters (2)
  • scalar for allowable change in control inputs
    User-provided scalar that bounds the step size in control inputs between iterations.
  • scalar for allowable change in objective
    User-provided scalar that bounds the change in the performance objective between iterations.

pith-pipeline@v0.9.0 · 5444 in / 1245 out tokens · 40059 ms · 2026-05-10T14:43:14.743366+00:00 · methodology

discussion (0)

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