Shown in Figure 1 below are the feed equilibrium conditions. Expressed is equilibrium CO conversion and CH4, CO, and CO2 effluent composition conditions as a function of temperature, on a dry basis. Other than water, hydrogen is the only other product component and its effluent composition is not shown. The significant temperature influence on product slate can be seen in Figure 1. At 450℃ the CH4 equilibrium composition and CO conversion are 61.6% and 92.57%, respectively. While at 250℃the CH4