反应蒸馏
萃取蒸馏
工艺工程
生化工程
化学
蒸馏
色谱法
工程类
作者
Eduardo Sánchez‐Ramírez,Shirui Sun,Jia Yi Sim,Ao Yang,Zong Yang Kong,Juan Gabriel Segovia‐Hernández
标识
DOI:10.1016/j.seppur.2024.127184
摘要
Existing studies on reactive-extractive distillation (RED) commonly misapply optimization variables by including reaction stages. Given the uncatalyzed nature of ethylene oxide (EO) hydration in RED, where it naturally occurs throughout the column, a more appropriate strategy is to optimize only the total stages, allowing the reactive stage to align accordingly. However, previous attempts to implement this approach faced challenges. Here we introduce an algorithm addressing the variable overlap issue in optimizing RED, exemplified in two case studies. In Case 1, we explored a distinct scenario where the original process designated a specific reaction zone. Adjustments were made to ensure the reaction occurred throughout the entire column but it leads to a 13 % total annual cost (TAC) increase compared to the base case. In Case 2, optimization was applied to a system where reaction were distributed throughout the column without prior optimization, yielding a marginal 3.87 % reduction in the TAC.
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