TY - JOUR
T1 - Process modelling integrated with interpretable machine learning for predicting hydrogen and char yield during chemical looping gasification
AU - Sison, A.E
AU - Etchieson, S.A
AU - Güleç, F
AU - Epelle, E.I
AU - Okolie, J.A
N1 - Funding Information:
Surprisingly, the effect of OC on hydrogen and char yield seems to be quite low compared to temperature. A similar experimental result have been documented in literature (Samprón et al., 2022; Wang et al., 2020). For instance, some researchers reported the impact of Fe-OC content (10, 20, and 25 wt% as Fe2O3) of three synthetic oxygen carriers supported on alumina during biomass CLG (Samprón et al., 2022). It was observed that the Fe content in the OC did not have a relevant effect on tar removal at any temperature or operating condition. Another study showed that the OC to fuel/biomass ratio had a slight impact on H2 production compared to temperature during CLG (Wang et al., 2020). There could be several explanations for this phenomenon. There is a possibility that the amount of OC present in the system is sufficient to attain optimum fuel conversion to produce H2 (OC saturation). Therefore, a further increase would not influence H2 and char production. Another explanation could be the mass transfer limitations. The gas-solid reactions in CLG are influenced by the mass transfer between the solid fuel and the OC particles. If the mass transfer is the limiting factor, rather than the availability of the OC, increasing the quantity of the oxygen carrier may not significantly impact the yields of hydrogen and char.The authors would like to thank the Honors College at the University of Oklahoma for the support and training provided to Arnold E. Sison as an undergraduate Honors student. Special appreciation to the Department of Chemical, Biological and Materials Engineering at the University of Oklahoma for providing the Aspen plus simulation used for the study. The authors also appreciate Philemon Udom and Meshach Tabat for their technical expertise and help with the process simulation.
Publisher Copyright:
© 2023 Elsevier Ltd
PY - 2023/8/15
Y1 - 2023/8/15
N2 - Chemical looping gasification (CLG) is a promising thermochemical process for the production of H2. CLG process is mainly based on oxygen transfer from an air reactor to a gasification reactor using solid metal oxides (also called oxygen carriers, (OC)) as oxidants. The unique oxygen separation system of CLG makes it an advanced process with a smaller carbon footprint compared to the conventional gasification process. The other advantages of CLG includes increased efficiency, reduced greenhouse gas emissions, and improved process stability compared to conventional biomass gasification. Although CLG is a promising technology, it still faces several challenges such as high capital cost, OC durability, complex reaction mechanism and scalability issues. Some of these challenges can be addressed by understanding the impact of various process conditions on H2 yield and char formation during CLG. The present study proposes a novel integrated process simulation and experimental studies to generate large dataset used for interpretable machine learning (ML) analysis. Three different ML models including support vector machine (SVM), random forest (RF), and gradient boost regression (GBR) were used to develop models for predicting the H2 and char yield during CLG. The GBR outperformed other models for the prediction of H2 and char yield during CLG with R2 value > 0.9. Among the experimental conditions, the temperature (T) and steam to biomass ratio (SBR) were the most relevant parameters affecting H2 and char production. Biomass ash, C, volatile matter (VM) and H content also influenced H2 and char formation. Overall, a combination of SHAP and partial dependence plot helped address the black box challenges of ML models.
AB - Chemical looping gasification (CLG) is a promising thermochemical process for the production of H2. CLG process is mainly based on oxygen transfer from an air reactor to a gasification reactor using solid metal oxides (also called oxygen carriers, (OC)) as oxidants. The unique oxygen separation system of CLG makes it an advanced process with a smaller carbon footprint compared to the conventional gasification process. The other advantages of CLG includes increased efficiency, reduced greenhouse gas emissions, and improved process stability compared to conventional biomass gasification. Although CLG is a promising technology, it still faces several challenges such as high capital cost, OC durability, complex reaction mechanism and scalability issues. Some of these challenges can be addressed by understanding the impact of various process conditions on H2 yield and char formation during CLG. The present study proposes a novel integrated process simulation and experimental studies to generate large dataset used for interpretable machine learning (ML) analysis. Three different ML models including support vector machine (SVM), random forest (RF), and gradient boost regression (GBR) were used to develop models for predicting the H2 and char yield during CLG. The GBR outperformed other models for the prediction of H2 and char yield during CLG with R2 value > 0.9. Among the experimental conditions, the temperature (T) and steam to biomass ratio (SBR) were the most relevant parameters affecting H2 and char production. Biomass ash, C, volatile matter (VM) and H content also influenced H2 and char formation. Overall, a combination of SHAP and partial dependence plot helped address the black box challenges of ML models.
U2 - 10.1016/j.jclepro.2023.137579
DO - 10.1016/j.jclepro.2023.137579
M3 - Article
SN - 0959-6526
VL - 414
JO - Journal of Cleaner Production
JF - Journal of Cleaner Production
M1 - 137579
ER -