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REVIEWNATpage 19holdREVIEW_MISSING_SOLUTIONP3UNREVIEWED

type=NAT · page=19–20 · marks=1 · content_conf=0.7999999999999999 · math_conf=0.807

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Consider the flowsheet in the figure for manufacturing 𝐶 via the reaction A+B→C in an isothermal

CSTR. The split in the separator is perfect so that the recycle stream is free of 𝐶 and the product stream is pure 𝐶. Let 𝑥𝑖 denote the mole fraction of species i (i=A, B, C) in the CSTR, which is operated in excess

.

k_x = /frac{5.0 /text{kmol}}{(m^3h).}

Pure ARecycle/Rkmol/h

Only A and B PureB CSTR Vm^3 rot

A+B→Cara

(−rₐ)=kₓxₐpeSxB=4

x_a

.

.

.

.

G_{/mathrm{ATE}}2025

Chemical Engineering

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Category: REVIEW_MISSING_SOLUTION · Priority: P3 · Disposition: source_limitation

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Source PDF: source.pdf

Segment	Page	BBox	Asset	Equation	Link
stem	19	`—`	`—`none	`—`	`REVIEW`
stem	19	`—`	`—`none	`—`	`REVIEW`
stem	19	`[357.475341796875,459.2207946777344,412.2815856933594,470.62078857421875]`	`—`none	`—`	`REVIEW`
stem	19	`—`	`—`none	`—`	`REVIEW`
stem	19	`—`	`—`none	`—`	`REVIEW`
stem	19	`—`	`—`none	`—`	`REVIEW`
stem	19	`[72.02400207519531,642.016357421875,544.5399780273438,656.4039916992188]`	`—`none	`—`	`REVIEW`
stem	19	`—`	`—`none	`—`	`REVIEW`
stem	19	`—`	`—`none	`—`	`REVIEW`

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