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Consider a first-order reaction ... in a real reactor where chemical reaction and dispersion are occurring. The Demonstration plots the ratio ... of the volumes of the real and plug flow reactors as a function of ... , where ... is the reactor's conversion. You can change the value of the dispersion dimensionless group ... , where ... is the dispersion coefficient due to axial mixing, ... is the reactor's length, and ... is the fluid's velocity. With ... near zero one recovers the plug flow behavior. As ... , the behavior of a mixed flow reactor is observed.
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