id	author	title	date	pages	extension	mime	words	sentence	flesch	summary	cache	txt
cet-15087		cet-15087		6	.pdf	application/pdf	2804	128	53	Conclusions This study has demonstrated that the assimilation of a variable overall heat transfer coefficient (UOR) in a non- isothermal model simulation of steam methane reforming (SMR) improves the predictive accuracy of the simulation for both packed-bed reactors (PBR) and membrane reactors (MR) Results show that membrane reactors outperform PBRs by reaching a higher methane conversion under similar operating conditions. Mathematical Model Reaction Kinetics In general, steam methane reforming is modeled through three key global reactions: methane reforming reaction (Endothermic): CH4 +	cache/cet-15087.pdf	txt/cet-15087.txt