5.(5 pts.) GasAdissolves in a beaker of stagnant liquidB, and reacts withBto formC(RA=-kprimeprimeprime1cA).Sketchplots ofcAas a function ofzfor both small and largekprimeprimeprime1. Here,zis the distance below the liquid/gas interface.6.(5 pts.) A material (A) is diffusing (no convection) into a porous cylinder (radiusR, lengthL) from a flowingfluid (B). The concentration of speciesAwithin the fluidiscA(r, θ, z, t), and the diffusivity within the fluidisDAB. Using this information, write an integral expression for the total rate of transport of speciesAfromthe fluid into the cylinder (molesA/time). You may assume thatAis dilute so that the total concentration isconstant, and that transport at the cylinder ends may be neglected.3