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The alternate application of a batch rectifier and a batch stripper is also studied.
This article proposes a nonlinear control strategy for a batch rectifier.
This contribution focuses on the development of a dynamic conceptual model for a batch rectifier having an infinite number of stages without resorting to multistage calculations.
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In the first part of the present work, the design approach of the ASE scheme in two different forms, namely ASE1 and ASE2, has been addressed for a batch reactive rectifier.
The analysis is done for both the conventional batch rectifier and the multivessel batch column.
Besides studying the well known batch configurations (rectifier, stripper, middle vessel column) we also suggest two novel configurations such as double column batch rectifier (DCBR) and double column batch stripper (DCBS).
In this contribution, a novel heat integrated distillation column (HIDiC) is proposed for batch rectifiers.
For conventional batch rectifiers, it is shown that there exists a limiting value rtop of the reflux ratio above which there is a 'sensitive' operating region characterized by a linear increase of the sensitivity function with respect to the concentration of the heavy component in the reboiler; the higher the reflux ratio, the wider this sensitive operating region.
Three column arrangements are considered: batch rectifiers, batch strippers and total-reflux columns.
For batch strippers, it is found that sensitive and non-sensitive operating regions are located somewhat symmetrically with respect to the case of batch rectifiers.
"I made a batch.
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