A system-level dynamic model for gasification process: Steady-state experimental validation and load-change predictions

The expansion of variable renewables creates a need for conversion technologies that can operate flexibly. Bubbling Fluidized Bed (BFB) gasifiers are promising because of their thermal stability and fuel flexibility, yet their dynamic behaviour is poorly characterized. This study develops one of the first system-level dynamic model of a 450 BFB gasifier using the APROS dynamic simulation platform, which natively couples thermal-hydraulics, gas-solid interactions, and control logic for time-domain studies. The model, based on the pilot facility at the Technical University of Darmstadt, is validated against experimental steady-state measurements of riser temperature, pressure distribution, and product gas composition. Predictions show strong agreement, with temperature and pressure errors below 8% and 2%, respectively. Mean Absolute Error (MAE) and Root Mean Square Error (RMSE) values for temperature and pressure are also low (<3%). Despite employing simplified reaction kinetics, the model reproduces major product gas species with sufficient accuracy for energy system evaluation. The model is then applied to investigate part-load steady states and dynamic load transitions. Simulations demonstrate that the gasifier maintains stable hydrodynamics and syngas composition during load reductions and ramp-ups, with only moderate fluctuations in and ( , ). These findings establish one of the first credible dynamic frameworks for BFB gasification, offering testable predictions to support pilot-scale transient measurements, control design, and integration of gasification technologies into renewable-based hybrid energy systems. • Developed a dynamic process model of a BFB gasifier to address a key gap. • Incorporates core–annulus hydrodynamics, solids recirculation, staged injection. • Steady-state validation: <8% T error and <2% ΔP; product gas well captured. • Part-load steady states and load-change dynamics were systematically investigated. • Dynamic simulations show stable hydrodynamics and moderate fluctuations (e.g., ) during load changes..

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Publication Details

Journal
Energy
Published
2026-01-20
DOI
https://doi.org/10.1016/j.energy.2026.140136
Citations
2
Primary Topic
Granular flow and fluidized beds
Type
article
Field-Weighted Citation Impact
83.55
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article

A system-level dynamic model for gasification process: Steady-state experimental validation and load-change predictions

Falah Alobaid, Mohammad Hossein Jamalkhoo, Juha Kaikko, Prof. Dr.-Ing. Bernd Epple et al.
2 citations
Energy
Granular flow and fluidized beds
83.55
article

A system-level dynamic model for gasification process: Steady-state experimental validation and load-change predictions

Falah Alobaid, Mohammad Hossein Jamalkhoo, Juha Kaikko, Prof. Dr.-Ing. Bernd Epple, Jens Martin Kaltenmorgen
article en
2 citations

Abstract

The expansion of variable renewables creates a need for conversion technologies that can operate flexibly. Bubbling Fluidized Bed (BFB) gasifiers are promising because of their thermal stability and fuel flexibility, yet their dynamic behaviour is poorly characterized. This study develops one of the first system-level dynamic model of a 450 BFB gasifier using the APROS dynamic simulation platform, which natively couples thermal-hydraulics, gas-solid interactions, and control logic for time-domain studies. The model, based on the pilot facility at the Technical University of Darmstadt, is validated against experimental steady-state measurements of riser temperature, pressure distribution, and product gas composition. Predictions show strong agreement, with temperature and pressure errors below 8% and 2%, respectively. Mean Absolute Error (MAE) and Root Mean Square Error (RMSE) values for temperature and pressure are also low (<3%). Despite employing simplified reaction kinetics, the model reproduces major product gas species with sufficient accuracy for energy system evaluation. The model is then applied to investigate part-load steady states and dynamic load transitions. Simulations demonstrate that the gasifier maintains stable hydrodynamics and syngas composition during load reductions and ramp-ups, with only moderate fluctuations in and ( , ). These findings establish one of the first credible dynamic frameworks for BFB gasification, offering testable predictions to support pilot-scale transient measurements, control design, and integration of gasification technologies into renewable-based hybrid energy systems. • Developed a dynamic process model of a BFB gasifier to address a key gap. • Incorporates core–annulus hydrodynamics, solids recirculation, staged injection. • Steady-state validation: <8% T error and <2% ΔP; product gas well captured. • Part-load steady states and load-change dynamics were systematically investigated. • Dynamic simulations show stable hydrodynamics and moderate fluctuations (e.g., ) during load changes..

EnergyVol. 344
Technische Universität Darmstadt (DE), Lappeenranta-Lahti University of Technology (FI)
Affordable and clean energy
Openalex Percentile: Top 0%
Granular flow and fluidized beds
83.55
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