International Journal of Hydrogen Energy, Vol.42, No.22, 15096-15106, 2017
Steam reforming of liquefied natural gas (LNG) for hydrogen production over nickel-boron-alumina xerogel catalyst
A series of mesoporous nickel-boron-alumina xerogel (x-NBA) catalysts with different boron/nickel molar ratio (x = 0-1) were prepared by an epoxide-driven sol gel method. The effect of boron/nickel molar ratio on the catalytic activities and physicochemical properties of nickel-boron-alumina xerogel catalysts was investigated in the steam reforming of liquefied natural gas (LNG). All the mesoporous x-NBA catalysts showed similar surface area. Introduction of boron increased interaction between nickel and support. In addition, introduction of boron into x-NBA catalysts reduced methane activation energy and increased nickel surface area. Promotion of boron had a positive effect on the catalytic activity due to the increase of adsorbed methane and nickel surface area. The amount of adsorbed methane and nickel surface area exhibited volcano-shaped trends with respect to boron/nickel molar ratio. LNG conversion and hydrogen yield increased with increasing the amount of adsorbed methane and with increasing nickel surface area. Among the catalysts, 0.3-NBA, which retained the largest amount of adsorbed methane and the highest nickel surface area, showed the best catalytic performance. It was also revealed that x-NBA catalysts showed strong coke resistance during the steam reforming reaction. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
Keywords:Steam reforming of LNG;Hydrogen production;Mesoporous nickel-boron-alumina catalyst;Epoxide-driven sol-gel method