Real time optimization of distillation columns using data‐driven models

Abstract This work presents a data‐driven model of a two‐product distillation tower that is suitable for real‐time optimization (RTO) of distillation columns. The proposed model accurately predicts product mass fractions using operating variables and tray temperatures by integrating a linear data‐driven inferential composition model (based on two tray temperatures in each section of the tower, reflux/distillate ratio, and reboiler duty/bottoms flow ratio) with a neural network (NN) model that predicts tray temperatures from the value of the manipulated variables. RTO is carried out via an iterative procedure where the sensitivity matrix is initially calculated from the model and updated using plant measurements from subsequent values. A butane splitter column is presented as a case study. Our results show that the implementation of the data‐driven model‐based RTO results in a solution that is within 0.1% of the optimization solution based on the rigorous tray‐to‐tray distillation simulation.

Authors

Institutions

Publication Details

Journal
The Canadian Journal of Chemical Engineering
Published
2024-11-03
DOI
https://doi.org/10.1002/cjce.25543
Citations
1
Primary Topic
Advanced Control Systems Optimization
Type
article
Field-Weighted Citation Impact
0.33

Funders

Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Real time optimization of distillation columns using data‐driven models

Prashant Mhaskar, Carlos Rodriguez, Vladimir Mahalec
1 citations
The Canadian Journal of Chemical Engineering
Advanced Control Systems Optimization
0.33
article

Real time optimization of distillation columns using data‐driven models

Prashant Mhaskar, Carlos Rodriguez, Vladimir Mahalec
article en
1 citations

Abstract

Abstract This work presents a data‐driven model of a two‐product distillation tower that is suitable for real‐time optimization (RTO) of distillation columns. The proposed model accurately predicts product mass fractions using operating variables and tray temperatures by integrating a linear data‐driven inferential composition model (based on two tray temperatures in each section of the tower, reflux/distillate ratio, and reboiler duty/bottoms flow ratio) with a neural network (NN) model that predicts tray temperatures from the value of the manipulated variables. RTO is carried out via an iterative procedure where the sensitivity matrix is initially calculated from the model and updated using plant measurements from subsequent values. A butane splitter column is presented as a case study. Our results show that the implementation of the data‐driven model‐based RTO results in a solution that is within 0.1% of the optimization solution based on the rigorous tray‐to‐tray distillation simulation.

The Canadian Journal of Chemical EngineeringVol. 103(6)
McMaster University (CA)
NOVA Chemicals, Imperial Oil Limited, Honeywell, Natural Sciences and Engineering Research Council of Canada
Openalex Percentile: Top 40%
Advanced Control Systems Optimization
0.33
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.