1.- Obtain the conversion that will be obtained in a tubular reactor 90 cm long and  in. in diameter using the same flows used in the CSTR reactor.

2.- Calculate the conversion that would be obtained in said reactor with another flow model (eg laminar)

3.- Calculate for said reactor NRe, NR and NPe.

Where NPe is the Peclet number defined as uL / DL where u is the linear velocity, L is the length of the considered segment, DL is the linear diffusivity in said segment

Flujo Distn 1.0 Flujo laminar 0.8 Flujo perfectamente mezclado 0.6 Conversin, x 0.4 NA KETE KYk21 "T ke: Constante cintica de primer orden 0.2 0.0 0.0 20 4.0 6.0 8.0 Numero de Reaccin, NR Nz = 2kZT/Umax = k