Acetaldehyde is synthesized by the catalytic dehydrogenation of ethanol:  C2H5OH=CH3CHO+H2 Fresh feed (pure ethanol) is blended with a recycle stream (95 mole% ethanol and 5% acetaldehyde), and the combined stream is heated and vaporized, entering the reactor at 280°C. Gases leaving the reactor are cooled to condense the acetaldehyde and unreacted ethanol. Off-gas from the condenser is sent to a scrubber, where the uncondensed organic compounds are removed and hydrogen is recovered as a by-product. The condensate from the condenser, which is 45 mole% ethanol, is sent to a distillation column that produces a distillate containing 99 mole% acetaldehyde and a bottoms product that constitutes the recycle blended with fresh feed to the process. The production rate of the distillate is 1000 kg/h. The pressure throughout the process may be taken as 1 atm absolute. If the fresh feed to the system flows at 23.4 kmol/h, the condensate flow rate is 42.6 kmol/h, and the single-pass conversion of ethanol in the reactor is 54.6%, calculate the flow rates of ethanol and hydrogen leaving in the reactor effluent (kmol/h).

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
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Acetaldehyde is synthesized by the catalytic dehydrogenation of ethanol: 

C2H5OH=CH3CHO+H2


Fresh feed (pure ethanol) is blended with a recycle stream (95 mole% ethanol and 5%
acetaldehyde), and the combined stream is heated and vaporized, entering the reactor at 280°C.
Gases leaving the reactor are cooled to condense the acetaldehyde and unreacted ethanol. Off-gas
from the condenser is sent to a scrubber, where the uncondensed organic compounds are
removed and hydrogen is recovered as a by-product. The condensate from the condenser, which
is 45 mole% ethanol, is sent to a distillation column that produces a distillate containing 99
mole% acetaldehyde and a bottoms product that constitutes the recycle blended with fresh feed
to the process. The production rate of the distillate is 1000 kg/h. The pressure throughout the
process may be taken as 1 atm absolute.

If the fresh feed to the system flows at 23.4 kmol/h, the condensate flow rate is 42.6 kmol/h, and
the single-pass conversion of ethanol in the reactor is 54.6%, calculate the flow rates of ethanol
and hydrogen leaving in the reactor effluent (kmol/h). 

Feed: C₂H5OH(1)
CONDENSER
REACTOR
Reactor
output: H₂,
C₂H5OH(v),
CH,CHO(v)
Recycle
95 mole% C₂H₂OH(1)
5 mole% CH3CHO(1)
Off-gas
to scrubber
Condensate
45 mole% C₂H5OH(1)
55 mole% CH3CHO(1)
CONDENSER
Distillate
99 mole% CH3CHO(1)
DISTILLATION
COLUMN
REBOILER
Transcribed Image Text:Feed: C₂H5OH(1) CONDENSER REACTOR Reactor output: H₂, C₂H5OH(v), CH,CHO(v) Recycle 95 mole% C₂H₂OH(1) 5 mole% CH3CHO(1) Off-gas to scrubber Condensate 45 mole% C₂H5OH(1) 55 mole% CH3CHO(1) CONDENSER Distillate 99 mole% CH3CHO(1) DISTILLATION COLUMN REBOILER
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