Process intensification in a methanol steam reforming chemical reactor with enhanced momentum transport Junjie Chen Department of Energy and Power Engineering, School of Mechanical and Power Engineering, Henan Polytechnic University, 2000 Century Avenue, Jiaozuo, Henan, 454000, P.R. China Contributor: Junjie Chen, ORCID: 0000-0001-5055-4309, E-mail address: komcjj@gmail.com Consideration must be given to the rate at which each step in the planned sequence occurs. In many instances, a desired reaction is possible in principle but in practice takes place so slowly as to be ineffective. It is then necessary to investigate whether the rate can be increased to a practicable level by altering the conditions of the reaction, for example, by raising the temperature or by adding an extra species, called a catalyst, that increases the rate without altering the course of the reaction. Streamwise distance (millimeters), Oxidation channel centerline temperature (degrees kelvin) 0 376.499 0.00025 391.55 0.0005 411.347 0.00075 432.857 0.001 451.349 0.00125 465.437 0.0015 475.536 0.00175 482.591 0.002 487.466 0.00225 490.805 0.0025 493.063 0.00275 494.556 0.003 495.508 0.00325 496.074 0.0035 496.366 0.00375 496.469 0.004 496.424 0.00425 496.278 0.0045 496.077 0.00475 495.832 0.005 495.555 0.00525 495.26 0.0055 494.955 0.00575 494.646 0.006 494.337 0.00625 494.033 0.0065 493.735 0.00675 493.445 0.007 493.164 0.00725 492.894 0.0075 492.635 0.00775 492.386 0.008 492.15 0.00825 491.925 0.0085 491.712 0.00875 491.511 0.009 491.323 0.00925 491.146 0.0095 490.98 0.00975 490.825 0.01 490.682 0.01025 490.549 0.0105 490.427 0.01075 490.314 0.011 490.212 0.01125 490.119 0.0115 490.036 0.01175 489.96 0.012 489.893 0.01225 489.833 0.0125 489.781 0.01275 489.737 0.013 489.699 0.01325 489.668 0.0135 489.643 0.01375 489.624 0.014 489.61 0.01425 489.603 0.0145 489.6 0.01475 489.601 0.015 489.607 0.01525 489.618 0.0155 489.632 0.01575 489.651 0.016 489.673 0.01625 489.699 0.0165 489.728 0.01675 489.76 0.017 489.796 0.01725 489.834 0.0175 489.875 0.01775 489.918 0.018 489.964 0.01825 490.012 0.0185 490.063 0.01875 490.115 0.019 490.169 0.01925 490.225 0.0195 490.283 0.01975 490.343 0.02 490.404 0.02025 490.467 0.0205 490.531 0.02075 490.597 0.021 490.663 0.02125 490.731 0.0215 490.8 0.02175 490.869 0.022 490.94 0.02225 491.011 0.0225 491.083 0.02275 491.155 0.023 491.228 0.02325 491.301 0.0235 &nbsp

Contributor: Junjie Chen, ORCID: 0000-0001-5055-4309, E-mail address: komcjj@gmail.com, Department of Energy and Power Engineering, School of Mechanical and Power Engineering, Henan Polytechnic University, 2000 Century Avenue, Jiaozuo, Henan, 454000, P.R. China