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Design and optimization study on a novel active/inactive catalyst particle multi-zone mixing fixed packed bed for cost-efficient solar-driven hydrogen production

  • Xi'an Jiaotong University
  • Ltd

Research output: Contribution to journalArticlepeer-review

Abstract

For more cost-efficient solar-driven hydrogen production in parabolic trough solar receiver-reactor systems, a novel active/inactive catalyst particle multi-zone mixing fixed packed bed is designed and optimized in this paper. Inspired by multi-physics mismatched coupling relationship revealed, the locally separately decoupling interfaces between active and inactive catalyst multi-zones were proposed to regulate the spatial thermal-chemical matching relationship. A three-dimensional isothermal surface fitting method was proposed to determine the multi-zone mixing interfaces. Corresponding novel multi-stages systems were further designed and optimized. The results show that the novel system can effectively improve the spatial thermal-chemical matching relationship by locally reusing inactive catalysts. The nearly optimal three-stages novel system saves 48.3% of the original active catalyst filling in a more cost-efficient yet safe way, which greatly improves the hydrogen production per unit mass of active catalyst by 82.26% under the sintering temperature limit. It provides a new regulating idea for similar solar-driven thermochemical applications.

Original languageEnglish
Article number156534
JournalInternational Journal of Hydrogen Energy
Volume257
DOIs
StatePublished - 5 Aug 2026

UN SDGs

This output contributes to the following UN Sustainable Development Goals (SDGs)

  1. SDG 7 - Affordable and Clean Energy
    SDG 7 Affordable and Clean Energy

Keywords

  • Hydrogen production
  • Inactive catalyst reusage
  • Methanol steam reforming reaction
  • Mixed filling method
  • Solar receiver-reactor
  • Thermal-chemical matching

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