(1) Boreskov Institute of Catalysis, Prosp. Akad. Lavrentieva 5;(2) Sobolev Institute of Mathematics, Prosp. Akad. Koptyuga 4, 630090 Novosibirsk, Russia
Abstract:
Using single catalyst pellets (5 mm) 15% Ptγ–Al2O3, we experimentally studied gas-phase benzene hydrogenation at normal pressure by thermocouple measurements of gas flow and
the pellet center. Temperature of gas flow was varied in the range of 20 ‡C / 350 ‡C for three molar fractions of benzene
vapor (0.1, 0.2, and 0.3) mixed with hydrogen. The ignition/extinction behavior of the flow-pellet temperature rise (maximum
values up to 100 ‡C/ 200 dgC) is explained by internal-external mass transport limitations of the reaction rate and reaction
reversibility at high pellet temperature. A simplified pseudobinary treatment of both multicomponent intrapellet mass transfer
(in bimodal porous media) and multicomponent external mass transfer (under forced convection) is proposed on the basis of
the analytical estimation. The validity of the suggested approach is confirmed by comparing the experimental data for benzene
hydrogenation with rigorous (multicomponent) and approximated (pseudobinary) calculations obtained by using a mathematical
model of a spherically symmetric pellet. The simplified approach appears to be quite accurate for reactions A+nH2=B of hydrogenation (n>0) or dehydrogenation (n<0) of sufficiently heavy compounds, i.e. if DAH≈DBH>>DAB