Deep regeneration of activated carbon catalyst and autothermal analysis for chemical looping methane thermo-catalytic decomposition process. (13th September 2018)

• Record Type: Journal Article
• Authors: Yang, Li; Liu, Fang; Liu, Yang; Quan, Wenbin; He, Jianlong
• Is Part Of: International journal of hydrogen energy. Volume 43:Number 37(2018)
• Page Start: 17633
• Page End: 17642
• Publication Date: 2018-09-13
• Subjects: Chemical looping methane decomposition -- Activated carbon -- Catalytic activity -- Heat balance; Hydrogen as fuel -- Periodicals; Hydrogène (Combustible) -- Périodiques; Hydrogen as fuel; Periodicals; 665.81
• DOI: 10.1016/j.ijhydene.2018.07.202
• Languages: English
• ISSNs: 0360-3199

Abstract

Abstract: The application of a chemical looping process to methane thermo-catalytic decomposition using activated carbon (AC) as a catalyst has been recognized as a promising technology for continuous high-purity H2 production in a carbon constrained world. However, it usually needs an external heat supply for the endothermic decomposition reactions. By taking advantage of the chemical looping combustion (CLC) technology, this study proposed a deep regeneration approach using H2 O and O2 as regeneration agents to overcome the issues with maintaining catalytic activity and producing the heat needed for the endothermic reactions of H2 production from methane. TG-DTA and bench scale fluidized bed experimental results indicate that a deep regeneration degree of 30% or above could completely reactivate the spent AC catalyst and simultaneously generate sufficient heat than required in the methane decomposition reaction. Characterization study implies that the deep regenerated AC catalyst could maintain its physical properties within a certain number of cycles. Based on the experimental results, the chemical looping methane thermo-catalytic decomposition process was further optimized and assessed by Aspen Plus ® thermodynamic simulation. The results indicate that heat and mass balances could be attained, and the circulation of the AC catalyst with a temperature difference of 262 °C between the decomposer and the regenerator enabling the process to run autothermally. Highlights: Use of CO2 or O2 or H2 O by themselves cannot meet needed catalyst regeneration. Deep regeneration using H2 O + O2 was suitable for AC activity resumption. A deep regenerated AC catalyst could maintain its physical properties. An autothermal process for continuous high purity H2 production was proposed. Thermodynamic modeling suggested heat and mass balances could be attained.