The following problems involving chemical-reaction stoichiometry are to be solved through the use of reaction coordinates. (a)

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The following problems involving chemical-reaction stoichiometry are to be solved through the use of reaction coordinates.

(a) Feed to a gas-phase reactor comprises 50 kmol·h−1 of species A, and 50 kmol·h−1 of species B. Two independent reactions occur:

A + B → C (I) A + C → D (II)

Analysis of the gaseous effluent shows mole fractions yA = 0.05 and yB =0.10.

(i) What is the reactor effluent rate in kmol·h−1 ?
(ii) What are the mole fractions yC and yD in the effluent?

(b) Feed to a gas-phase reactor comprises 40 kmol·h−1 of species A, and 40 kmol·h−1 of species B. Two independent reactions occur:

A + B → C (I) A + 2B → D (II)

Analysis of the gaseous effluent shows mole fractions: yC = 0.52 and y= 0.04.

Determine the rates (kmol·h−1) of all species in the effluent stream.

(c) Feed to a gas-phase reactor is 100 kmol·h−1 of pure species A. Two independent reactions occur:

A → B + C (I) A + B → D (II)

Reaction (I) produces valuable species C and coproduct B. The side reaction (II) produces by-product D. Analysis of the gaseous effluent shows mole fractions yC = 0.30 and yD = 0.10. Determine the rates (kmol·h−1) of all species in the effluent stream.

(d) The feed to a gas-phase reactor is 100 kmol·h−1, containing 40 mol-% species A and 60 mol-% species B. Two independent reactions occur:

A + B → C (I) A + B → D + E (II)

Analysis of the gaseous effluent shows mole fractions y= 0.25 and y= 0.20. Determine:

(i) Rates in kmol·h−1 of all species in the effluent stream.
(ii) Mole fractions of all species in the effluent stream.

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Introduction To Chemical Engineering Thermodynamics

ISBN: 9781259696527

8th Edition

Authors: J.M. Smith, Hendrick Van Ness, Michael Abbott, Mark Swihart

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