Title of article
Design and control of reactive distillation–recovery distillation flowsheet with a decanter for synthesis of N-propyl propionate
Author/Authors
Xu، نويسنده , , Hong and Ye، نويسنده , , Qing and Zhang، نويسنده , , Hao-Li Qin، نويسنده , , Jiwei and Li، نويسنده , , Ning، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2014
Pages
10
From page
38
To page
47
Abstract
Reactive distillation (RD) for the synthesis of n-propyl propionate (ProPro) is operated with an excess of the reactant n-propyl alcohol (ProOH). It is simulated as a two-column system which can be easily controlled compared with a single reactive column which is operated neat, because the recovery column acts conceptually as a composition analyzer. The optimal steady-state design of the two-column system with the minimal total annual cost (TAC) is screened first. Then, an effective control scheme is established to handle feed disturbances. Only tray temperatures are required in the dynamic control two-column process. The product purity is held close to the set value 99.5 mol% and large deviation is prevented.
Keywords
dynamic control , n-Propyl propionate , Reactive distillation
Journal title
Chemical Engineering and Processing: Process Intensification
Serial Year
2014
Journal title
Chemical Engineering and Processing: Process Intensification
Record number
1611705
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