L 1[m] "Reactor length" Ra 0.1[m] "Reactor radius" E 75362[J/mol] "Activation energy" A 16.96e12[1/h] "Frequency factor" Diff 1e-9[m^2/s] "Diffusion coefficient" unit 1/1[m] "Axisymmetric unit conversion" v0 v_w0+v_po0+v_m0 "Total flow rate" cA0 n_po0/v0 "Propylene oxide concentration, inlet" cB0 n_w0/v0 "Water concentration, inlet" cMe0 n_m0/v0 "Methanol concentration, inlet" rho0 (cA0*M_po+cB0*M_w+cMe0*M_m) "Density at inlet" M_po 58.095[g/mol] "Molar weight, propylene oxide" M_m 32.042[g/mol] "Molar weight, methanol" M_w 18[g/mol] "Molar weight, water" rho_po_p 830[kg/m^3] "Density, propylene oxide" rho_m_p 791.3[kg/m^3] "Density, methanol" rho_w_p 1000[kg/m^3] "Density, water" v_ratio 3.5 "Ratio water flow rate / (prop+me) flow rate" n_po0 0.1[mol/s] "Molar flow rate po in" n_m0 v_po0*rho_m_p/M_m "Molar flow rate m in" v_po0 n_po0*M_po/rho_po_p "Volumetric flow rate po in" v_m0 v_po0 "Volumetric flow rate m in" v_w0 v_ratio*(v_po0+v_m0) "Volumetric flow rate w in" n_w0 rho_w_p*v_w0/M_w "Molar flow rate w in" mc 0.1[kg/s] "Mass flow rate, cooling fluid"