Thermal Runaway Incident Database Summary Report (2018–2023)
The Thermal Runaway Incident Database Summary Report (2018–2023) is a curated, anonymized compilation of real-world thermal runaway incidents in chemical process industries, designed to support hazard identification, risk assessment, and process safety improvement. It documents root causes, contributing factors, operational conditions, and mitigation outcomes across diverse reaction systems—including batch, semi-batch, and continuous processes. The report serves as an evidence-based learning resource for chemical engineers, process safety professionals, and regulatory bodies to prevent recurrence through pattern recognition and systemic analysis.
📖 Overview
📑 Key Components
🎯 Applications
- ✓ Process Hazard Analysis (PHA) and What-If/HAZOP facilitation
- ✓ Development of site-specific thermal safety management standards
- ✓ Benchmarking of reaction calorimetry and RC1/ARC test protocols against real-world failure modes
📐 Key Formulas
Adiabatic Temperature Rise (ΔT_ad)
ΔT_ad = (−ΔH_r × X) / (Σ m_i × C_p,i)
Calculates maximum temperature increase assuming no heat loss; where ΔH_r is enthalpy of reaction, X is conversion, m_i and C_p,i are mass and specific heat of components.
Time to Maximum Rate under Adiabatic Conditions (TMR_ad)
TMR_ad = (E_a / R) × (1 / T_onset − 1 / T_max)
Estimates time for reaction rate to peak under zero-heat-removal conditions; derived from Arrhenius kinetics and used to assess emergency response window.
Maximum Temperature of Synthesis Reaction (MTSR)
MTSR = T_initial + ΔT_ad × (1 − α)
Predicts highest temperature reached if cooling fails mid-reaction; α is fractional conversion at failure initiation.