Syngas production in a novel methane dry reformer by utilizing of tri-reforming process for energy supplying: Modeling and simulation

A comparative study of CO2 utilization in methanol synthesis with various syngas production technologies

“…Moreover, since trireforimg is a relatively new technology, to the best of our knowledge, complete reaction kinetics are currently unavailable in the literature. Recent publications related to the modeling aspect of trireforimg include the work from Farniaei et al [35]. In that study, Farniaei et al developed a comprehensive model for a packed-bed trireformer.…”

“…For SMR and DMR reactions, the authors used steady-state kinetics on a Ni catalyst reported by Xu and Froment [33], while for methane total oxidation, the kinetics for a Pt-based catalyst reported in Trimm and Lam [36] were modified to be compatible with a Ni-based catalyst. Unfortunately, the PO reaction, which is an essential reaction path for producing heat, CO and H 2 , was not included in Farniaei et al [35]. Because of this lack in the literature, the Gibbs reactor model in Aspen Plus is used to simulate the reformer in this scenario.…”

Thermodynamic analysis of dry reforming of CH4 with CO2 at high pressures

“…The principal objective of DRM studies has therefore been to develop suitable catalysts with good lifetime stability. DRM is a highly endothermic reaction in which large amount of energy is required (Farniaei et al, 2014;Agrafiotis et al, 2014). The unavoidable water formation as the side product indirectly reduces the syngas selectivity and lowers the H 2 /CO ratio (Bradford and Vannice, 1996;Larentis et al, 2001).…”

Kinetic and CFD Modeling of Exhaust Gas Reforming of Natural Gas in a Catalytic Fixed‐Bed Reactor for Spark Ignition Engines

“…These kinetic models are commonly used by many researchers today for the reforming processes that involve steam reforming, dry reforming, and partial and complete oxidation, such as tri and autothermal reforming (Eqs. –) , : …”