Non-porous polyether sulfone hollow fibers(with a 5 μm poly(dimethylsiloxane)coating)were used as structured packing in the distillation of ethanol-water solutions.In this novel membrane contactor,liquid flowed throu...Non-porous polyether sulfone hollow fibers(with a 5 μm poly(dimethylsiloxane)coating)were used as structured packing in the distillation of ethanol-water solutions.In this novel membrane contactor,liquid flowed through the lumens of the fibers,and vapor flowed countercurrently outside the fibers.The results showed that the new membrane contactor gave better,more productive separations than traditional packing in distillation.The minimal HETP of hollow fibers could reach as low as 5.8 cm,and the contactor worked well above the limit where flooding normally occurs in conventional cases.The overall mass-transfer coefficient and individual mass-transfer coefficients based on the gas side and liquid side were calculated respectively.The theoretical analysis indicated that the resistance in the liquid was responsible for more than half of the total resistance.展开更多
The enthalpies of dilution of L serine in ethanol water mixtures (with 0.05 increments ranging from 0.05 to 0.40 ethanol by weight) have been measured with LKB 2277 Bio Activity Monitor at 298.15 K.Calculations show t...The enthalpies of dilution of L serine in ethanol water mixtures (with 0.05 increments ranging from 0.05 to 0.40 ethanol by weight) have been measured with LKB 2277 Bio Activity Monitor at 298.15 K.Calculations show that the value of pairwise enthalpic interaction coefficients h2 is negative and minimized at 0.25 ethanol in mixtures.展开更多
利用Aspen Plus模拟软件,建立了分离丙酮-乙醇-水物系的隔壁塔工艺流程。在保证丙酮产品纯度不低于99.2%的前提下,使用响应面法分析了隔壁塔的结构参数对能耗的影响,拟合出塔结构参数与再沸器热负荷的二次方程,对隔壁塔的结构参数进行...利用Aspen Plus模拟软件,建立了分离丙酮-乙醇-水物系的隔壁塔工艺流程。在保证丙酮产品纯度不低于99.2%的前提下,使用响应面法分析了隔壁塔的结构参数对能耗的影响,拟合出塔结构参数与再沸器热负荷的二次方程,对隔壁塔的结构参数进行了优化。优化结果为:预分离段、公共精馏段、公共提馏段和侧线采出段的理论塔板数分别为22,20,19,18;预分离段的进料位置为第16塔板,公共提馏段的再沸器热负荷为405.63 k W。验证结果显示,优化结果与模拟结果的相对误差为0.65%,说明流程模拟与响应面法相结合用于隔壁塔结构参数的优化可行。与传统工艺相比,隔壁塔分离工艺的设备费用降低26.86%、年度总费用降低41.10%。展开更多
文摘Non-porous polyether sulfone hollow fibers(with a 5 μm poly(dimethylsiloxane)coating)were used as structured packing in the distillation of ethanol-water solutions.In this novel membrane contactor,liquid flowed through the lumens of the fibers,and vapor flowed countercurrently outside the fibers.The results showed that the new membrane contactor gave better,more productive separations than traditional packing in distillation.The minimal HETP of hollow fibers could reach as low as 5.8 cm,and the contactor worked well above the limit where flooding normally occurs in conventional cases.The overall mass-transfer coefficient and individual mass-transfer coefficients based on the gas side and liquid side were calculated respectively.The theoretical analysis indicated that the resistance in the liquid was responsible for more than half of the total resistance.
文摘The enthalpies of dilution of L serine in ethanol water mixtures (with 0.05 increments ranging from 0.05 to 0.40 ethanol by weight) have been measured with LKB 2277 Bio Activity Monitor at 298.15 K.Calculations show that the value of pairwise enthalpic interaction coefficients h2 is negative and minimized at 0.25 ethanol in mixtures.
文摘利用Aspen Plus模拟软件,建立了分离丙酮-乙醇-水物系的隔壁塔工艺流程。在保证丙酮产品纯度不低于99.2%的前提下,使用响应面法分析了隔壁塔的结构参数对能耗的影响,拟合出塔结构参数与再沸器热负荷的二次方程,对隔壁塔的结构参数进行了优化。优化结果为:预分离段、公共精馏段、公共提馏段和侧线采出段的理论塔板数分别为22,20,19,18;预分离段的进料位置为第16塔板,公共提馏段的再沸器热负荷为405.63 k W。验证结果显示,优化结果与模拟结果的相对误差为0.65%,说明流程模拟与响应面法相结合用于隔壁塔结构参数的优化可行。与传统工艺相比,隔壁塔分离工艺的设备费用降低26.86%、年度总费用降低41.10%。
