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Gas-liquid mass transfer parameters in benzoic acid oxidation process.

机译:苯甲酸氧化过程中的气液传质参数。

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Benzoic acid oxidation process is an intermediate step in the commercial production of phenol through toluene oxidation using air. In this process, phenol can be easily oxidized to undesirable by-products; and the overall reaction rate can be controlled by gas-liquid mass transfer.; In this study, the solubility (C*) volumetric mass transfer coefficients (kLa) and gas-liquid interfacial area (a) for oxygen and nitrogen in molten benzoic acid and mixtures were measured in one-liter agitated reactor operating in gas-inducing (GIR) and surface-aeration (SAR) modes under typical industrial conditions. The effects of mixing speed, temperature, pressure, and magnesium and copper benzoate concentrations on the mass transfer parameters in both reactor types were statistically investigated.; The C* values for both gases were found to increase with temperature and pressure while the effect of MgBz and CuBz concentrations on C* values for both gases was insignificant. The kLa values obtained for both gases in both reactor types using the transient physical gas absorption technique were statistically correlated with a confidence level >95%. The diameter of gas bubbles, mass transfer coefficients, and gas holdup were also calculated. The kLa values were found to significantly increase with mixing speed and slightly increase with pressure and temperature. The kLa values appeared to slightly increase with Mg benzoate concentration in the GIR while the values increased and then decreased in the SAR. The kL a values for both gases in the GIR were always higher than those in the SAR; and under similar operating conditions, kLa values for N2 were higher than or equal to those of O2.; The gas-liquid interfacial areas for O2 and N2 in benzoic acid containing copper and magnesium benzoates were obtained using a physical and a chemical method. The addition of CuBz and MgBz to benzoic acid significantly affected the gas-liquid interfacial areas due to the changes of the liquid phase properties. Also, the gas-liquid interfacial areas obtained using the chemical method were consistently smaller than those obtained with the physical method.
机译:苯甲酸氧化工艺是通过使用空气进行甲苯氧化进行苯酚商业化生产的中间步骤。在这个过程中,苯酚很容易被氧化成不希望的副产物。总反应速率可通过气液传质来控制。在这项研究中,在熔融苯甲酸和混合物中,溶解度(C *)的体积传质系数(k a)和氧气和氮气在气液界面面积(a)的测量方法如下:在典型的工业条件下,以气体诱导(GIR)和表面曝气(SAR)模式运行的1升搅拌反应器。统计研究了两种反应器类型中混合速度,温度,压力以及苯甲酸镁和苯甲酸铜浓度对传质参数的影响。发现两种气体的C *值均随温度和压力的升高而增加,而MgBz和CuBz浓度对两种气体的C *值的影响均不显着。使用瞬态物理气体吸收技术获得的两种反应器中两种气体的k L 值在统计上与置信度> 95%相关。还计算了气泡的直径,传质系数和气体滞留率。发现k L 值随混合速度显着增加,而随压力和温度略有增加。 GIR中k L 的值似乎随苯甲酸镁的浓度而略有增加,而SAR中的值则先升高后降低。 GIR中两种气体的k L a值始终高于SAR中的k L a值;在相似的工作条件下,N 2 的k L a值大于或等于O 2 的值。采用物理和化学方法获得了含苯甲酸铜和镁的苯甲酸中O 2 和N 2 的气液界面面积。由于液相性质的变化,在苯甲酸中添加CuBz和MgBz会显着影响气液界面面积。而且,使用化学方法获得的气液界面面积始终小于使用物理方法获得的气液界面面积。

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