Kinetics and thermal effects on particle reaction rates in hydrolysis of the copper–chlorine cycle

The copper-chlorine (Cu–Cl) cycle is a promising thermochemical water-splitting process for hydrogen production. In this paper, CuCl 2 solid particles in the hydrolysis reaction of the Cu–Cl cycle are examined over a range of operating temperatures and steam-to-copper ratios. A shrinking core model (SCM) is used to analyse the particle conversion process. Experiments are also conducted within a vertical semi-batch fixed bed reactor. Dried particles have the lowest overall conversion, compared to crushed or crystallised samples. Further X-ray diffraction (XRD) examination examined the reaction products between 370 and 400 °C. Activation energies ranged from 32 to 54 kJ/mol. This paper establishes a direct correlation between reduction of the steam-to-copper ratio and subsequent conversion. The results provide useful new insight into the hydrolysis reaction of the Cu–Cl cycle. • Cu–Cl cycle hydrolysis varies by temperature and steam-to-copper ratio. • Crushed CuCl 2 has the highest conversion rate, while dried samples the lowest. • The activation energies for the hydrolysis reaction range from 32 to 54 kJ/mol.

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Publication Details

Journal
International Journal of Hydrogen Energy
Published
2025-05-05
DOI
https://doi.org/10.1016/j.ijhydene.2025.04.485
Citations
3
Primary Topic
Chemical Looping and Thermochemical Processes
Type
article
Field-Weighted Citation Impact
2.02

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article

Kinetics and thermal effects on particle reaction rates in hydrolysis of the copper–chlorine cycle

Kelly Hawboldt, Kevin Pope, G.F. Naterer, H.M. Radwan
3 citations
International Journal of Hydrogen Energy
Chemical Looping and Thermochemical Processes
2.02
article

Kinetics and thermal effects on particle reaction rates in hydrolysis of the copper–chlorine cycle

Kelly Hawboldt, Kevin Pope, G.F. Naterer, H.M. Radwan
article en
3 citations

Abstract

The copper-chlorine (Cu–Cl) cycle is a promising thermochemical water-splitting process for hydrogen production. In this paper, CuCl 2 solid particles in the hydrolysis reaction of the Cu–Cl cycle are examined over a range of operating temperatures and steam-to-copper ratios. A shrinking core model (SCM) is used to analyse the particle conversion process. Experiments are also conducted within a vertical semi-batch fixed bed reactor. Dried particles have the lowest overall conversion, compared to crushed or crystallised samples. Further X-ray diffraction (XRD) examination examined the reaction products between 370 and 400 °C. Activation energies ranged from 32 to 54 kJ/mol. This paper establishes a direct correlation between reduction of the steam-to-copper ratio and subsequent conversion. The results provide useful new insight into the hydrolysis reaction of the Cu–Cl cycle. • Cu–Cl cycle hydrolysis varies by temperature and steam-to-copper ratio. • Crushed CuCl 2 has the highest conversion rate, while dried samples the lowest. • The activation energies for the hydrolysis reaction range from 32 to 54 kJ/mol.

International Journal of Hydrogen EnergyVol. 134
Memorial University of Newfoundland (CA), University of Prince Edward Island (CA)
Canadian Nuclear Laboratories, Natural Sciences and Engineering Research Council of Canada
Clean water and sanitation
Openalex Percentile: Top 14%
Chemical Looping and Thermochemical Processes
2.02
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Kinetics and thermal effects on particle reaction rates in hydrolysis of the copper–chlorine cycle — Kelly Hawboldt, Kevin Pope, et al. · International Journal of Hydrogen Energy (2025) | TGRS Research Map | TGRS