Estimate the volume of a plug-flow reactor (in m3) required for production of ethylene from ethane (C,H, →C,H, + H,) based on the following data and assumptions: a. The feed is pure ethane at 1 kg s', 1000K and 2 bar (abs). b. The reaction is first-order and irreversible at low conversion, with k = 0.254 s-' at 1000 K. c. The reactor is operated isothermally and isobarically. d. Conversion of ethane is 20% at the outlet.

Introduction to Chemical Engineering Thermodynamics
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Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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Estimate the volume of a plug-flow reactor (in m3) required for
production of ethylene from ethane (C,H, → C,H, + H,) based on
the following data and assumptions:
a. The feed is pure ethane at 1 kg s-', 1000K and 2 bar (abs).
b. The reaction is first-order and irreversible at low conversion, with
k = 0.254 s- at 1000 K.
c. The reactor is operated isothermally and isobarically.
d. Conversion of ethane is 20% at the outlet.
Transcribed Image Text:Estimate the volume of a plug-flow reactor (in m3) required for production of ethylene from ethane (C,H, → C,H, + H,) based on the following data and assumptions: a. The feed is pure ethane at 1 kg s-', 1000K and 2 bar (abs). b. The reaction is first-order and irreversible at low conversion, with k = 0.254 s- at 1000 K. c. The reactor is operated isothermally and isobarically. d. Conversion of ethane is 20% at the outlet.
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