Avoiding runaway scenarios in Fischer-Tropsch synthesis during startup: temperature and pressure influence

The operation of Fischer-Tropsch synthesis (FTS) pilot plants is essential to advancing Power-to-X strategies. However, conducting experimental campaigns with multiple startups introduces significant challenges due to the system's pronounced sensitivity to thermal instability and remains an unaddressed challenge in the literature. This experimental study analyzes the thermal response of a pilot-scale FTS reactor under controlled heating and pressurization, aiming to identify safe operating limits to prevent thermal runaway. In this experimental work, runaway was observed when the heating rate response (HRR) exceeded 15 ºC/h, while stable operation was achieved by limiting oil heating to <1 ºC/h. Pressurization from 10 to 20 bar at 3 bar/h induced a significantly lower thermal rate of 0.48 ºC/bar, offering an alternative to thermal ramping below 210 ºC. These findings highlight the importance of combining temperature and pressure ramping strategies to maintain thermal control during startup and underscore the need to evaluate the heating rate response continuously and maintain it below the critical threshold to ensure safe and stable operation.

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Publication Details

Journal
Process Safety and Environmental Protection
Published
2025-09-10
DOI
https://doi.org/10.1016/j.psep.2025.107849
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
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article

Avoiding runaway scenarios in Fischer-Tropsch synthesis during startup: temperature and pressure influence

Martí Biset‐Peiró, Andrés A. García Blanco, Jordi Guilera, Karen Quintana
Process Safety and Environmental Protection
Catalysts for Methane Reforming
article

Avoiding runaway scenarios in Fischer-Tropsch synthesis during startup: temperature and pressure influence

Martí Biset‐Peiró, Andrés A. García Blanco, Jordi Guilera, Karen Quintana
article en

Abstract

The operation of Fischer-Tropsch synthesis (FTS) pilot plants is essential to advancing Power-to-X strategies. However, conducting experimental campaigns with multiple startups introduces significant challenges due to the system's pronounced sensitivity to thermal instability and remains an unaddressed challenge in the literature. This experimental study analyzes the thermal response of a pilot-scale FTS reactor under controlled heating and pressurization, aiming to identify safe operating limits to prevent thermal runaway. In this experimental work, runaway was observed when the heating rate response (HRR) exceeded 15 ºC/h, while stable operation was achieved by limiting oil heating to <1 ºC/h. Pressurization from 10 to 20 bar at 3 bar/h induced a significantly lower thermal rate of 0.48 ºC/bar, offering an alternative to thermal ramping below 210 ºC. These findings highlight the importance of combining temperature and pressure ramping strategies to maintain thermal control during startup and underscore the need to evaluate the heating rate response continuously and maintain it below the critical threshold to ensure safe and stable operation.

Process Safety and Environmental ProtectionVol. 203
Institut de Recerca en Energia de Catalunya (ES), Universitat de Barcelona (ES)
Openalex Percentile: Top 86%
Catalysts for Methane Reforming
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