Liquid-Solid Mass Transfer for Cocurrent Gas-Liquid Upflow Through Solid Foam Packings

This article presents the liquid solid mass transfer characteristics for cocurrent upflow operated gas liquid solid foam packings. Aluminum foam was used with 10, 20, and 40 pores per linear inch (PPI), coated with 5 wt % Pd on gamma-alumina. The effects of gas velocity (u(g) = 0.1-0.8 m(g)(3) m(r)(-2) s(-1)) and liquid velocity (u(t) = 0.02 and 0.04 m(t)(3) m(r)(-2) s(-1)) are studied using the Pd/Bi catalyzed oxidation of glucose. The volumetric liquid solid mass transfer coefficient, k(Is)a(Is), is approximately the same for 10 PPI and 20 PPI solid foams, ranging from 2 x 10(-2) to 9 x 10(-2) m(t)(3) m(r)(-3) s(-1). For 40 PPI solid foam, somewhat I lower values for k(Is)a(Is) were found, ranging from 6 x 10(-3) to 4 x 10(-2) m(t)(3) m(r)(-3) s(-1). The intrinsic liquid solid mass transfer coefficient, k(Is), increases with increasing liquid velocity and was found to be proportional to u(t)(0.98). Initially, k(Is) decreases with increasing gas velocity and after reaching a minimum value increases with increasing gas velocity. The values for k(Is) range from 5.5 x 10(-6) to 8 x 10(-4) m(t)(3) m(i)(-2) s(-1), which is in the same range as found for random packings and corrugated sheet packings. (C) 2010 American Institute of Chemical Engineers AIChE. J, 56: 2923-2933, 2010