Example 5.5 Propane is dehydrogenated to form propylene in a catalytic reactor: C,H. C,H. + H2 The process is to be designed for a 95% overall conversion of propane. The reaction products are separated into two streams: the first, which contains H, CHe, and 0.555% of C,Ha that leaves the reactor, is taken off as product; the second, which contains the balance of the unreacted propane and 5% of the propylene in the first stream, is recycled to the reactor. Calculate (a) the composition of the product, (b) the ratio: (moles recycled)/(moles fresh feed), and (c) the "single-pass" conversion. CaHa-n. Mixing point Fresh Feed- REACTOR SEPARATOR CSHe na CSHe na Ha ns CaHene CH n Ha ne 100 g-mol CaH. Recycle CHe na CHe ne

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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Example 5.5 Propane is dehydrogenated to form propylene in a catalytic reactor:
C,H. -
C,H. + H2
The process is to be designed for a 95% overall conversion of propane. The reaction products are
separated into two streams: the first, which contains H2, C,H, and 0.555% of C,Ha that leaves the
reactor, is taken off as product; the second, which contains the balance of the unreacted propane
and 5% of the propylene in the first stream, is recycled to the reactor.
Calculate (a) the composition of the product, (b) the ratio: (moles recycled)/(moles fresh feed), and
(c) the "single-pass" conversion.
CaHe
Mixing point
SEPARATOR
Fresh Feed
100 g-mol CaH.
REACTOR
CSHe = na
CHe = n
H- ns
CaHe
CHe - n
Ha = ne
ne
Recycle
CaHe=ne
Transcribed Image Text:Example 5.5 Propane is dehydrogenated to form propylene in a catalytic reactor: C,H. - C,H. + H2 The process is to be designed for a 95% overall conversion of propane. The reaction products are separated into two streams: the first, which contains H2, C,H, and 0.555% of C,Ha that leaves the reactor, is taken off as product; the second, which contains the balance of the unreacted propane and 5% of the propylene in the first stream, is recycled to the reactor. Calculate (a) the composition of the product, (b) the ratio: (moles recycled)/(moles fresh feed), and (c) the "single-pass" conversion. CaHe Mixing point SEPARATOR Fresh Feed 100 g-mol CaH. REACTOR CSHe = na CHe = n H- ns CaHe CHe - n Ha = ne ne Recycle CaHe=ne
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