Feasibility of Batch Reactive Distillation with Equilibrium-Limited Consecutive Reactions in Rectifier, Stripper, or Middle-Vessel Column

<table>Simulated and calculated profiles at total reboil ratio, at <svg height="11.1" id="M124" style="vertical-align:-0.17555pt" version="1.1" viewbox="0 0 38.887501 11.1" width="38.887501" xmlns="http://www.w3.org/2000/svg">
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<tspan style="font-size: 12.50px; " x="0" y="0">𝑅</tspan>
<tspan style="font-size: 12.50px; " x="12.715551" y="0">=</tspan>
<tspan style="font-size: 12.50px; " x="24.755939" y="0">5</tspan>
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</svg> and at <svg height="14.725" id="M125" style="vertical-align:-3.24037pt" version="1.1" viewbox="0 0 69.137497 14.725" width="69.137497" xmlns="http://www.w3.org/2000/svg">
<g transform="matrix(1.25,0,0,-1.25,0,14.725)">
<g transform="translate(72,-60.22)">
<text transform="matrix(1,0,0,-1,-71.95,63.5)">
<tspan style="font-size: 12.50px; " x="0" y="0">𝐹</tspan>
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<tspan style="font-size: 8.75px; " x="0" y="0">𝑑</tspan>
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<tspan style="font-size: 12.50px; " x="0" y="0">/</tspan>
<tspan style="font-size: 12.50px; " x="3.4758339" y="0">𝑉</tspan>
<tspan style="font-size: 12.50px; " x="14.12839" y="0">=</tspan>
<tspan style="font-size: 12.50px; " x="26.168779" y="0">0</tspan>
<tspan style="font-size: 12.50px; " x="32.42028" y="0">.</tspan>
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International Journal of Chemical Engineering

fig11

Figure 11

Figure 11: Feasibility of Batch Reactive Distillation with Equilibrium-Limited Consecutive Reactions in Rectifier, Stripper, or Middle-Vessel Column 