Analysis of Dynamic Characteristics of Reconfigurable Modular Reactor Systems for Renewable Methanol Synthesis

A modular production system for renewable methanol synthesis is one viable way for simultaneously realizing scalable storage of renewable energy and carbon dioxide utilization. It is crucial to improve the dynamic performances of the modular reactor systems to rapidly adapt to fluctuations of renewable energy and increase the methanol yield. In this work, four configurations and their dynamic characteristics of reactors in series and parallel were investigated to elucidate the impacts of reactor configurations on the performances of reconfigurable modular reactors, in which a 2-D transient model of fixed-bed reactors for methanol synthesis was established. The dynamic characteristics of the reactor systems during startup, shutdown, disturbance, and switching were explored. The results indicated that modular reactors in series are preferred when the feed rate is less than two times the rated flow rate in a single reactor, whereas modular reactors in parallel are favorable when the feed rate exceeds six times the rated flow rate. The modular reactors in series and parallel are much more favorable for the feed rates in between. The startup and shutdown times of the reactor systems are significantly affected by the stage numbers of the reactors and the feed flow rate in a single reactor. In general, the startup and shutdown times increase with the increase of stage number and the decrease of flow rates of the reactors. The response time to flow rate fluctuations of the reactor system is mainly determined by the stage number of the reactor and the flow rate of a single reactor. Fewer stage numbers and higher flow rates lead to a rapid response. The mode switching time between different configurations is also intimately related to the flow rates. Larger flow rates result in a relatively short residence time and a rapid switching process. These results provide insights into the optimal design and operation of modular reactor systems for renewable methanol production.

Authors

Institutions

Publication Details

Journal
Industrial & Engineering Chemistry Research
Published
2024-10-17
DOI
https://doi.org/10.1021/acs.iecr.4c02818
Citations
5
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
0.53

Funders

Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Analysis of Dynamic Characteristics of Reconfigurable Modular Reactor Systems for Renewable Methanol Synthesis

Lixia Kang, Xin Gao, Yongzhong Liu, Xinshan Kong
5 citations
Industrial & Engineering Chemistry Research
Catalysts for Methane Reforming
0.53
article

Analysis of Dynamic Characteristics of Reconfigurable Modular Reactor Systems for Renewable Methanol Synthesis

Lixia Kang, Xin Gao, Yongzhong Liu, Xinshan Kong
article en
5 citations

Abstract

A modular production system for renewable methanol synthesis is one viable way for simultaneously realizing scalable storage of renewable energy and carbon dioxide utilization. It is crucial to improve the dynamic performances of the modular reactor systems to rapidly adapt to fluctuations of renewable energy and increase the methanol yield. In this work, four configurations and their dynamic characteristics of reactors in series and parallel were investigated to elucidate the impacts of reactor configurations on the performances of reconfigurable modular reactors, in which a 2-D transient model of fixed-bed reactors for methanol synthesis was established. The dynamic characteristics of the reactor systems during startup, shutdown, disturbance, and switching were explored. The results indicated that modular reactors in series are preferred when the feed rate is less than two times the rated flow rate in a single reactor, whereas modular reactors in parallel are favorable when the feed rate exceeds six times the rated flow rate. The modular reactors in series and parallel are much more favorable for the feed rates in between. The startup and shutdown times of the reactor systems are significantly affected by the stage numbers of the reactors and the feed flow rate in a single reactor. In general, the startup and shutdown times increase with the increase of stage number and the decrease of flow rates of the reactors. The response time to flow rate fluctuations of the reactor system is mainly determined by the stage number of the reactor and the flow rate of a single reactor. Fewer stage numbers and higher flow rates lead to a rapid response. The mode switching time between different configurations is also intimately related to the flow rates. Larger flow rates result in a relatively short residence time and a rapid switching process. These results provide insights into the optimal design and operation of modular reactor systems for renewable methanol production.

Industrial & Engineering Chemistry ResearchVol. 63(43)
Advanced Energy Systems (United States) (US), Shaanxi University of Chinese Medicine (CN), Xi'an Jiaotong University (CN)
National Natural Science Foundation of China
Affordable and clean energy
Openalex Percentile: Top 42%
Catalysts for Methane Reforming
0.53
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.