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首页> 外文期刊>Journal of Chemical Technology & Biotechnology >Separation of p-xylene from ternary xylene mixture using silicalite-1membrane: process optimization studies
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Separation of p-xylene from ternary xylene mixture using silicalite-1membrane: process optimization studies

机译:使用silicalite-1膜从三甲苯混合物中分离对二甲苯的工艺优化研究

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摘要

BACKGROUND: The design of experiments (DoE) is applied to the process optimization of p-xylene (pX) separation from its isomers m-xylene (mX) and o-xylene (oX) mixture using silicalite-1 membrane supported on α-alumina. A central composite design (CCD) coupled with response surface methodology (RSM) was used to correlate the effect of two separation process variables, temperature (150–250 C) and pX feed partial pressure (0.10–0.26 kPa) to three responses: (i) pX flux; (ii) pX/oX separation factor; and (iii) pX/mX separation factor. The significant factors affecting each response were elucidated from the analysis of variance (ANOVA). The interaction between two variables was investigated systematically based on threedimensional response surface plots. RESULTS: The optimization criteria were used to maximize the value of pX flux, pX/mX separation factor and pX/oX separation factor. The optimum pX flux of 5.94 × 10-6 molm-2 s-1, pX/oX separation factor of 19 and pX/mX separation factor of 20 were obtained at a temperature of 198 C and pX feed partial pressure of 0.22 kPa. CONCLUSIONS: The experimental results were in good agreement with the simulated values obtained from the proposed models, with an average error of ±2.90%. In comparison with the conventional approach, DoE provides better flexibility of the process studies and a useful guideline for themembrane process operation for pX separation.
机译:背景:实验设计(DoE)用于将α-氧化铝上的silitelite-1膜从其异构体间二甲苯(mX)和邻二甲苯(oX)混合物中分离对二甲苯(pX)的工艺中, 。使用中央复合设计(CCD)和响应表面方法(RSM)来将两个分离过程变量(温度(150–250 C)和pX进料分压(0.10–0.26 kPa))的影响与三个响应相关联:( i)pX通量; (ii)pX / oX分离因子; (iii)pX / mX分离因子。通过方差分析(ANOVA)阐明了影响每个响应的重要因素。基于三维响应面图系统地研究了两个变量之间的相互作用。结果:优化标准用于最大化pX通量,pX / mX分离因子和pX / oX分离因子的值。在198°C的温度和0.22 kPa的pX进料分压下获得的最佳pX通量为5.94×10-6 molm-2 s-1,pX / oX分离系数为19,pX / mX分离系数为20。结论:实验结果与所提出模型的模拟值吻合良好,平均误差为±2.90%。与传统方法相比,能源部提供了更好的工艺研究灵活性,并为膜分离过程中膜工艺的操作提供了有用的指导。

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