Reactor Temperature Excursion Control With Early Warning Actions

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Solution Overview

Problem

Industrial processes, particularly those involving exothermic reactions like hydrocracking and hydrotreating, are prone to temperature excursions that can lead to costly shutdowns, equipment damage, and safety hazards due to uneven flow distribution, feed composition changes, and other factors, necessitating improved control systems to prevent and mitigate such incidents.

Innovation Solution

An enhanced control system with early warning mechanisms and automated actions to manage process variables, including quench gas distribution and reactor bed temperature control, to prevent temperature runaways and avoid emergency shutdowns, utilizing a multi-stage approach to stabilize operations.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If traditional control systems are used for exothermic reactions, then equipment simplicity is maintained, but temperature control precision deteriorates leading to excursions and shutdowns

Engineering Contradiction:
Improvetemperature control precisionVSAvoidcontrol system complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The system performs preliminary actions by continuously monitoring multiple temperature zones and process variables before temperature excursions occur. The control system detects early signs of thermal runaway and initiates corrective actions (adjusting feed rate, coolant flow, or reactor conditions) before the temperature exceeds safe limits, thereby preventing excursions rather than reacting to them after occurrence.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The control system implements multi-loop feedback mechanisms where temperature sensors in different reactor zones continuously feed data back to controllers that adjust process parameters. This closed-loop feedback ensures precise temperature control by constantly comparing actual temperatures with setpoints and making real-time corrections, resolving the contradiction between precision and complexity through intelligent control architecture.

Inventive Principle:
Principle #23Feedback

2Reliability

If early warning mechanisms are implemented, then reliability is improved, but device complexity increases

Engineering Contradiction:
Improveon-stream reliabilityVSAvoidcontrol system complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The early warning mechanism performs preliminary detection of incipient temperature excursions by monitoring rate of temperature change and comparing against predictive models. This allows the system to identify potential problems before they manifest as full-scale excursions requiring emergency shutdown, thereby improving reliability through proactive detection without requiring overly complex intervention systems.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The control system introduces an intermediary layer between temperature measurement and emergency shutdown - a predictive analysis module that processes temperature trends and process variables to generate early warnings. This intermediary layer filters normal fluctuations from actual threats, providing reliable early detection while maintaining system simplicity by only triggering alerts when genuine excursions are predicted.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Manufacturing precision

If automated control actions are taken, then temperature control precision is improved, but ease of operation deteriorates

Engineering Contradiction:
Improvetemperature control precisionVSAvoidsystem operation simplicity
Core Design Contradiction:
Manufacturing precisionVSEase of operation

Solution Approach 1:

The control system performs self-service by automatically detecting temperature deviations and executing corrective actions without operator intervention. The system monitors its own performance, compares actual temperatures with target values, and autonomously adjusts feed rate, coolant flow, or other process parameters to maintain precise temperature control, thereby achieving high precision while simplifying operator workload through self-regulation.

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

Automated feedback loops continuously measure temperature, compare with setpoints, and automatically adjust process parameters to maintain precision. This closed-loop control eliminates manual intervention for routine adjustments, improving temperature control precision while making the system easier to operate by removing the burden of constant manual monitoring and adjustment from operators.

Inventive Principle:
Principle #23Feedback

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

The system effectively reduces the risk of temperature excursions, minimizing downtime, equipment damage, and production losses by providing timely interventions and maintaining safe operating conditions, thus enhancing on-stream reliability.

Implementation Method 1

processes involving exothermic reactions like hydrocracking and hydrotreating

Methodology Applied
Scientific EffectExothermic reaction: Exothermic Reaction

Data Source

PatentEP3642678B1Incipient temperature excursion mitigation and control
Publication Date: 2026.02.25 UOP LLC
  • EP3642678B1 patent drawingFigure 1
  • EP3642678B1 patent drawingFigure 2
  • EP3642678B1 patent drawingFigure 2

AI summary

Systems and methods are disclosed for detecting temperature excursion in a chemical plant or petrochemical plant or refinery. Aspects of the disclosure provide an enhanced control system for a reactor, such as in hydroprocessing. The enhanced control system may provide early warnings of impending undesirable events, directly or indirectly manipulate certain process variables to reduce undesirable outcomes, and/or directly or indirectly manipulate of certain process variables so as to place a reactor unit in a "safe park" state. This may avoid a high temperature trip, depressuration, associated operating risks, allow for faster recovery from temperature excursions, and/or avoid unplanned emergency shutdowns of the reactor, chemical process, plant, or refinery.