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Multi-objective optimization of simultaneous oxidative desulfurization and denitrogenation of model fuel

二苯并噻吩 烟气脱硫 化学 中心组合设计 催化作用 响应面法 过氧化氢 硫黄 吡啶 超声 氮气 柴油 化学工程 色谱法 有机化学 工程类
作者
Snehlata Kumari,Sonali Sengupta
出处
期刊:Journal of Industrial and Engineering Chemistry [Elsevier BV]
卷期号:134: 457-473 被引量:1
标识
DOI:10.1016/j.jiec.2024.01.009
摘要

Petroleum fractions are accompanied with sulfur and nitrogen compounds, and nitrogen compounds tend to compete for the catalyst active sites, reducing desulfurization efficiency. They can be removed by oxidative desulfurization and denitrogenation, wherein the sulfur and nitrogen compounds are converted into corresponding oxides with higher polarity than their parent forms, thus favoring their extractive or adsorptive removal from the oil phase. The introduction of ultrasound into the oxidation system can significantly improve the process efficiency and oxidation kinetics through strong cavitation phenomena involving physical and chemical effects. In this work, ultrasound-assisted simultaneous oxidation of pyridine and dibenzothiophene (DBT) contained in a model fuel was performed. Response surface methodology (RSM) was employed to study the effect of six parameters, viz., catalyst dose (5–12.5 g/L), reaction time (5–60 min), ultrasonic amplitude (10–60 %), volume of hydrogen peroxide (0.5–2 mL), volume of acetic acid (0.5–2 mL) and reaction temperature (40–60 °C) on the conversion of DBT and pyridine. A face-centered central composite design was employed as the RSM tool, and the effect of the parameters and their interactions on the two responses was investigated. The two responses were simultaneously optimized via desirability functions and overlaying individual contour plots. The results revealed that sonication significantly enhanced the conversion of both compounds. All six factors significantly influenced the oxidation of pyridine, while DBT conversion was mainly affected by four factors. The desirability for the process under consideration ranged from 0.85 to 0.89, and at the optimum conditions, 100 % conversion of pyridine and 46.06 % conversion of DBT were obtained. Two-staged oxidation of the fuel at optimum conditions resulted in 100 and 93.7 % conversion of pyridine and DBT, respectively.

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