Several applications such as liquid-liquid extraction in micro-fluidic devices are concerned with the flow of two immiscible liquid phases. The commonly observed flow regimes in these systems are slug-flow and stratif...Several applications such as liquid-liquid extraction in micro-fluidic devices are concerned with the flow of two immiscible liquid phases. The commonly observed flow regimes in these systems are slug-flow and stratified flow. The latter regime in micro-channels has the inherent advantage that separation of the two liquids at the exit is efficient. Recently extraction in a stratified counter-current flow has been studied experimentally and it has been shown to be more efficient than co-current flow. An analytical as well as a numerical method to determine the steady-state solution of the corresponding convection-diffusion equation for the two flow-fields is presented. It is shown that the counter-current process is superior to the co-current process for the same set of parameters and operating conditions. A simplified model is proposed to analyse the process when diffusion in the transverse direction is not rate limiting. Different approaches to determining mass transfer coefficient are compared. The concept of log mean temperature difference used in design of heat exchangers is extended to describe mass transfer in the system.展开更多
The solvent of P350 was applied to extract and separate the oxalic acid from the mother-liquor originated from the precipitation of cobalt by oxalic acid,and its extraction mechanism was deduced.Some factors,including...The solvent of P350 was applied to extract and separate the oxalic acid from the mother-liquor originated from the precipitation of cobalt by oxalic acid,and its extraction mechanism was deduced.Some factors,including the concentration of P350, the concentration of hydrochloric acid and the concentration of oxalic acid were investigated to determine the best distribution coefficient of the oxalic acid.In the case of phase ratio(O/A)at 2.0,the extraction of the oxalic acid was more than 95%and its concentration in the extraction raffinate was lower than 0.004 0 mol/L after six-stage counter-current extraction.While the phase ratio(O/A)of the stripping was at 1.0,the recovery of oxalic acid attained more than 95%after ten-stage counter-current stripping.展开更多
研究不同温度和超声密度下循环超声提取玛咖生物碱的动力学及热力学。分别采用双指数模型和范特霍夫方程用于提取动力学过程拟合和热力学参数计算。结果表明双指数模型能较好的拟合玛咖生物碱提取过程,生物碱得率和速率常数随着温度或...研究不同温度和超声密度下循环超声提取玛咖生物碱的动力学及热力学。分别采用双指数模型和范特霍夫方程用于提取动力学过程拟合和热力学参数计算。结果表明双指数模型能较好的拟合玛咖生物碱提取过程,生物碱得率和速率常数随着温度或超声密度的增加而增加,洗涤和扩散阶段的活化能分别为16.41 k J/mol和17.52 k J/mol。循化超声提取过程是吸热、不可逆和自发的。与传统浸提相比,循环超声提取在20℃和50℃时,生物碱得率均显著高于传统浸提(p<0.01)。因此循环超声提取是一种高效的提取技术,可用于玛咖生物碱提取。展开更多
文摘Several applications such as liquid-liquid extraction in micro-fluidic devices are concerned with the flow of two immiscible liquid phases. The commonly observed flow regimes in these systems are slug-flow and stratified flow. The latter regime in micro-channels has the inherent advantage that separation of the two liquids at the exit is efficient. Recently extraction in a stratified counter-current flow has been studied experimentally and it has been shown to be more efficient than co-current flow. An analytical as well as a numerical method to determine the steady-state solution of the corresponding convection-diffusion equation for the two flow-fields is presented. It is shown that the counter-current process is superior to the co-current process for the same set of parameters and operating conditions. A simplified model is proposed to analyse the process when diffusion in the transverse direction is not rate limiting. Different approaches to determining mass transfer coefficient are compared. The concept of log mean temperature difference used in design of heat exchangers is extended to describe mass transfer in the system.
文摘The solvent of P350 was applied to extract and separate the oxalic acid from the mother-liquor originated from the precipitation of cobalt by oxalic acid,and its extraction mechanism was deduced.Some factors,including the concentration of P350, the concentration of hydrochloric acid and the concentration of oxalic acid were investigated to determine the best distribution coefficient of the oxalic acid.In the case of phase ratio(O/A)at 2.0,the extraction of the oxalic acid was more than 95%and its concentration in the extraction raffinate was lower than 0.004 0 mol/L after six-stage counter-current extraction.While the phase ratio(O/A)of the stripping was at 1.0,the recovery of oxalic acid attained more than 95%after ten-stage counter-current stripping.
文摘研究不同温度和超声密度下循环超声提取玛咖生物碱的动力学及热力学。分别采用双指数模型和范特霍夫方程用于提取动力学过程拟合和热力学参数计算。结果表明双指数模型能较好的拟合玛咖生物碱提取过程,生物碱得率和速率常数随着温度或超声密度的增加而增加,洗涤和扩散阶段的活化能分别为16.41 k J/mol和17.52 k J/mol。循化超声提取过程是吸热、不可逆和自发的。与传统浸提相比,循环超声提取在20℃和50℃时,生物碱得率均显著高于传统浸提(p<0.01)。因此循环超声提取是一种高效的提取技术,可用于玛咖生物碱提取。
