为了系统研究环氧乙烷水溶液失控反应热动力学参数的变化规律,采用等温扫描量热仪C600和绝热量热仪VSP-2分别对环氧乙烷水溶液进行了量热试验研究,得到了纯环氧乙烷的热稳定性数据,以及不同质量分数环氧乙烷水溶液的起始放热温度、最高...为了系统研究环氧乙烷水溶液失控反应热动力学参数的变化规律,采用等温扫描量热仪C600和绝热量热仪VSP-2分别对环氧乙烷水溶液进行了量热试验研究,得到了纯环氧乙烷的热稳定性数据,以及不同质量分数环氧乙烷水溶液的起始放热温度、最高放热温度和压力、放热量、绝热温升及失控反应过程的温度、压力变化等。结果表明,纯环氧乙烷发生失控反应的起始温度接近360℃,其放热量高达2 600 k J/kg。水加入环氧乙烷能够显著降低体系的起始放热温度至200℃以下。随环氧乙烷水溶液质量分数升高,失控反应致灾后果的严重程度明显提高。最高温度和压力、温升和压升速率、放热量及绝热温升随环氧乙烷质量分数升高而增大,而达到最大反应速率的时间减小。展开更多
The effect of different surfactants(n-octyltrimethylammonium bromide(OTABr),sodium dodecyl benzene sulfonate(SDBS) and Tween 80) with different critical micelle concentrations(CMC) on the CO_2 absorption into aqueous ...The effect of different surfactants(n-octyltrimethylammonium bromide(OTABr),sodium dodecyl benzene sulfonate(SDBS) and Tween 80) with different critical micelle concentrations(CMC) on the CO_2 absorption into aqueous solutions in a bubble column is analyzed in the present work.The presence of these surfactants increased the gas-liquid interfacial area,and decreased the liquid phase mass transfer coefficient,but with significant different extent.The results indicated that the CMC can be a key parameter affecting the mass transfer of CO_2 absorption into a dilute aqueous solution of a surfactant.Sardeing's model was used to fit the experimental data successfully by re-correlating the parameters.展开更多
文摘为了系统研究环氧乙烷水溶液失控反应热动力学参数的变化规律,采用等温扫描量热仪C600和绝热量热仪VSP-2分别对环氧乙烷水溶液进行了量热试验研究,得到了纯环氧乙烷的热稳定性数据,以及不同质量分数环氧乙烷水溶液的起始放热温度、最高放热温度和压力、放热量、绝热温升及失控反应过程的温度、压力变化等。结果表明,纯环氧乙烷发生失控反应的起始温度接近360℃,其放热量高达2 600 k J/kg。水加入环氧乙烷能够显著降低体系的起始放热温度至200℃以下。随环氧乙烷水溶液质量分数升高,失控反应致灾后果的严重程度明显提高。最高温度和压力、温升和压升速率、放热量及绝热温升随环氧乙烷质量分数升高而增大,而达到最大反应速率的时间减小。
基金Supported by the National Natural Science Foundation of China(20736005)
文摘The effect of different surfactants(n-octyltrimethylammonium bromide(OTABr),sodium dodecyl benzene sulfonate(SDBS) and Tween 80) with different critical micelle concentrations(CMC) on the CO_2 absorption into aqueous solutions in a bubble column is analyzed in the present work.The presence of these surfactants increased the gas-liquid interfacial area,and decreased the liquid phase mass transfer coefficient,but with significant different extent.The results indicated that the CMC can be a key parameter affecting the mass transfer of CO_2 absorption into a dilute aqueous solution of a surfactant.Sardeing's model was used to fit the experimental data successfully by re-correlating the parameters.
