Mayur Mundhwa

TL;DR: In this paper, four different configurations between segmented and continuously coated layers of combustion and reforming catalysts for hydrogen production by combustion assisted methane steam reforming (MSR) are studied in terms of reaction heat flux and reactor plate temperature distributions as well as in terms methane and hydrogen mole fraction distributions.

TL;DR: In this article, a numerical model is developed to predict the performance of a microchannel methanol steam reformer with different catalyst layer configurations to produce hydrogen-rich syngas for a high temperature polymer electrolyte membrane fuel cell (HT-PEMFC).

TL;DR: In this paper, the experimental measurements of the molar heat capacities of four aqueous physical solvents of importance in natural gas sweetening: tetramethylene sulfone (sulfolane), 4-formylmorpholine (NFM), 1-methyl-2-pyrrolidinone (NMP), and triethylene glycol dimethyl ether (TEGDME) were carried out in the temperature range of (303.15 to 353.15) K and for the entire range of mole fractions.

TL;DR: In this paper, the aqueous 2-((2-aminoethyl)amino)ethanol solutions were measured at six temperatures in the range (298.15 to 343.15) K and refractive indices at five temperature ranges (300 to 333.15 K).

TL;DR: In this paper, a parametric comparison study is carried out between segmented and conventional continuous layer configurations of the coated combustion-catalyst to investigate their influence on the performance of methane steam reforming (MSR) for hydrogen production in a catalytic plate reactor (CPR).