Reactive Absorption Control Using ML for Throughput and Energy Balance

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Solution Overview

Problem

Reactive absorption units face inefficiencies in controlling acid gas removal processes due to unmeasured parameters and imbalances, leading to suboptimal throughput and energy consumption, with potential gas breakthroughs.

Innovation Solution

Implementing a method that uses machine learning techniques, specifically 1D convolutional neural networks (1D-CNN) and kinetic models, to estimate missing parameters, reconcile data imbalances, and optimize control parameters for reactive absorption units, allowing for closed-loop or open-loop system control.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If traditional control methods are used for reactive absorption units, then the system operation is simple, but the throughput is suboptimal and energy consumption is high

Engineering Contradiction:
ImprovethroughputVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The patent implements a closed-loop control system that continuously monitors operating parameters (temperatures, pressures, flow rates) and uses this feedback to adjust control variables in real-time, optimizing throughput while minimizing energy consumption. The system compares actual measurements with model predictions and automatically adjusts operations to maintain optimal performance.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The optimization system dynamically adjusts operating parameters such as amine circulation rate, reboiler duty, and column pressures based on real-time conditions and economic objectives. By continuously changing these parameters to optimal values, the system maximizes throughput while minimizing energy consumption, resolving the contradiction between productivity and energy use.

Inventive Principle:
Principle #35Parameter changes

2Measurement precision

If more measurements and monitoring are implemented to improve control accuracy, then the measurement precision increases, but the device complexity increases

Engineering Contradiction:
Improveparameter measurement accuracyVSAvoidcontrol system complexity
Core Design Contradiction:
Measurement precisionVSDevice complexity

Solution Approach 1:

The patent introduces a process model as an intermediary that reconciles measurements from multiple sources and estimates unmeasured parameters. This model acts as a mediator between raw sensor data and control decisions, improving measurement precision by filling in missing information without requiring direct physical measurements for every parameter, thus avoiding excessive device complexity.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The system replaces physical measurement devices for unmeasured parameters with virtual measurements generated by the process model. Instead of installing additional sensors and measurement equipment (which would increase device complexity), the system uses mathematical models and data reconciliation to estimate parameters like acid gas loading and tray temperatures, achieving high measurement precision through computational methods.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

3Productivity

If real-time optimization calculations are performed to maximize throughput, then the productivity increases, but the computational requirements and system complexity increase

Engineering Contradiction:
Improvethroughput maximizationVSAvoidoptimization system complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The system performs preliminary actions by pre-calculating optimal operating trajectories and control strategies based on economic objectives and process constraints. The model predictive controller uses pre-developed process models and optimization algorithms to determine optimal control moves in advance, enabling real-time throughput maximization without requiring complex computational resources during actual operation.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The optimization system is designed to be dynamic and adaptive, adjusting its computational effort and optimization frequency based on process conditions and changes. The system dynamically recalculates optimal operations only when necessary, balancing throughput maximization with computational efficiency, thereby managing system complexity while maintaining high productivity.

Inventive Principle:
Principle #15Dynamics

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

Enhances operational efficiency by maximizing throughput and minimizing energy consumption while preventing gas breakthroughs, thereby improving the robustness and performance of reactive absorption units.

Implementation Method 1

a reboiler to provide heat energy to the stripper

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 2

An aqueous (typically amine) solution is circulated within the column and acts as an absorbent. The amine solution absorbs the acidic gases from the gas stream

Methodology Applied
Scientific EffectChemical absorption: Absorption (physical)

Implementation Method 3

the reboiler includes a steam control valve to adjust a duty cycle of the reboiler

Methodology Applied
Scientific EffectSteam flow control: Pressure Gradient

Data Source

PatentUS20250352941A1Real-time optimization of reactive absorption units
Publication Date: 2025.11.20 SAUDI ARABIAN OIL CO
  • US20250352941A1 patent drawing
  • US20250352941A1 patent drawing
  • US20250352941A1 patent drawing

AI summary

A system and method for controlling a reactive absorbance unit are provided. An exemplary method includes obtaining operating data for the reactive absorbance unit, reconciling data imbalances, and estimating unmeasured parameters. An optimization calculation is performed, and control parameters are adjusted based on the optimization calculation.