Reaction Rates and Interfacial Chemical Reactions

<p>Isothermal conditions</p> Signup and view all the answers

<p>External mass transport through the boundary layer</p> Signup and view all the answers

<p>The decrease in volume of unreacted core (-dV)</p> Signup and view all the answers

<p>The rate of diffusion to the reaction surface</p> Signup and view all the answers

<p>The shape of the particle</p> Signup and view all the answers

<p>Pore diffusion</p> Signup and view all the answers

<p>The pseudo-steady-state approximation</p> Signup and view all the answers

<p>$y = mx + b$</p> Signup and view all the answers

<p>$\frac{d^2C_b}{dx^2} - k_sSV C_b^n = 0$</p> Signup and view all the answers

<p>$A = lw$</p> Signup and view all the answers

<p>$C = 2\pi r$</p> Signup and view all the answers

<p>$A = \frac{1},{2}bh$</p> Signup and view all the answers

<p>$V = \pi r^2h$</p> Signup and view all the answers

<p>CSTR</p> Signup and view all the answers

<p>$𝐷𝑒 ∇2 𝐶𝑏 − 𝜈𝐴 = 0$</p> Signup and view all the answers

<p>$−𝜌𝐵 𝑑𝑟𝑐 𝑑𝑡 = 𝑏𝑘𝑠 𝐶𝑏$</p> Signup and view all the answers

<p>$𝑡 ∗ ≃ 𝑔𝐹𝑔 (𝑥) + 𝜎 2 𝑝𝐹𝑝 (𝑥)$</p> Signup and view all the answers

<p>$V \frac{dVC_A},{dt} = FiCA_i - FoCA_o + \int r_A dV$</p> Signup and view all the answers

<p>$V = F(CAi - CAo) - rA$</p> Signup and view all the answers

<p>$V \frac{dVC_A},{dt} = 0$</p> Signup and view all the answers

<p>Lower</p> Signup and view all the answers

<p>$V \frac{dVCA},{dt} = FiCAi - FoCAo + \int rA dV$</p> Signup and view all the answers

<p>Plug flow reactor</p> Signup and view all the answers

<p>$V = F(CAi - CAo) - rA$</p> Signup and view all the answers

<p>Plug flow reactor</p> Signup and view all the answers