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Mathematical modeling and optimization of industrial scale ELUXYL simulated moving bed (SMB)

机译:工业尺度Eluxyl模拟移动床的数学建模与优化(SMB)

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摘要

In this work, a detailed study on the modeling, simulation and optimization of the industrial-scale Eluxyl simulated moving bed (SMB) process are presented. Commercial SPX3000 (Ba-faujasite type zeolite) was used as an adsorbent, and para-diethylbenzene applied as a desorbent for separating para-xylene from other C-8 aromatics isomers. In the first step, the xylenes and para-diethylbenzene adsorption equilibrium on the commercial adsorbent were measured at operating conditions (175 degrees C, 9 bar) experimentally. The density of particle and porosities were determined from commercial plant operation and adsorbent analysis. Furthermore, mass transfer coefficients, including internal (diffusion in the pore) and external (diffusion in the liquid film) resistance, have been investigated in details. A common mathematical model encompassing the SMB strategy, node model, extended Langmuir isotherm, and rate expression were constructed to implement a numerical simulation of the industrial-scale Eluxyl SMB process with and without considering backwash stream. The accuracy of the mathematical model was validated by the industrial data. Besides, a dynamic optimization framework with Sequential Quadratic Programming (SQP) optimization algorithm was used for obtaining optimal conditions. Two separate single objective optimizations by considering minimum desorbent consumption and maximum SMB unit productivity as objectives were firstly designated. By comparing the results, it was concluded that minimizing desorbent consumption was more favorable to be selected as an objective function, which could achieve 6.35% increase in productivity and 7.28% decrease in desorbent consumption. Finally, two-level optimization was planned for reaching maximum feed throughput with minimum desorbent consumption. The results showed that productivity could be increased by 13.75%, and para-diethylbenzene consumption could be reduced by 10.81% at the optimal condition.
机译:在这项工作中,提出了对工业级榆木模拟移动床(SMB)工艺的建模,仿真和优化的详细研究。商业SPX3000(BA-FAUJASITE型沸石)用作吸附剂,并施加乙烯基苯基苯基苯,用于从其他C-8芳烃异构体中分离对二甲苯。在第一步中,在经过实验的操作条件(175℃,9巴)的操作条件下测量商业吸附剂上的二甲苯和乙烯基苯吸附平衡。从商业植物操作和吸附剂分析确定颗粒和孔隙率的密度。此外,已经研究了传质系数,包括内部(在孔中的扩散)和外部(在液体膜中扩散)电阻,细节已经研究。构建了包括SMB策略,节点模型,扩展Langmuir等温和速率表达的常见数学模型,以实现具有和不考虑反冲洗流的工业级精氨酸SMB过程的数值模拟。工业数据验证了数学模型的准确性。此外,使用具有顺序二次编程(SQP)优化算法的动态优化框架用于获得最佳条件。通过考虑最小解吸消耗和最大的SMB单位生产率,可以将两个单独的单个客观优化作为目标被指定为目标。通过比较结果,得出结论,最小化解吸剂消耗更有利于选择为目标函数,该函数可以达到6.35%的生产率提高,解吸剂消耗降低7.28%。最后,计划以最大的解吸消耗达到最大馈电量的两级优化。结果表明,生产率可以提高13.75%,并且可以在最佳条件下减少10.81%的乙基苯消耗。

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