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Influence of estimated physical constants and vapor pressure for esters in the methanol/ethanol recovery column for biodiesel production

机译:生物柴油生产估计物理常数和蒸气压在甲醇/乙醇回收塔中的影响

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摘要

The influence of the estimated values of the physical constants and vapor pressure of esters in a process simulation using the Aspen Hysys was evaluated from the energy parameters of a methanol/ethanol recovery distillation column of a biodiesel production plant. This study was necessary, because in process simulators most of FAMEs and FAEEs are not originally available in the simulator library, due to the lack of experimental data for these components. Accuracy analyses for the values of reboiler temperature and reboiler heat duty of the simulated column were performed from simulations using different predictive models and experimental data. Results demonstrated that small deviations of the vapor pressure can generate considerable errors in the reboiler temperature and reboiler heat duty. In addition, errors can be even greater if vapor pressure is estimated from inaccurate critical constants. Deviations up to 13% were observed for the reboiler temperature and up to 16% for the reboiler heat duty. It is demonstrated that reliable simulations and process design are strongly dependent on the selected physical properties of the esters, specially vapor pressure, which are generated from available experimental data and using group contribution and corresponding states models.
机译:从生物柴油生产厂的甲醇/乙醇回收蒸馏塔的能量参数评价使用ASPEN Hysys的工艺模拟中物理常数和酯蒸气压的影响。这项研究是必要的,因为在流程模拟器中,由于这些组件的实验数据缺乏实验数据,因此,大多数来自模拟器库最初不可用。使用不同的预测模型和实验数据,从模拟中进行模拟柱的再沸器温度和再沸器热占空比的精度分析。结果表明,蒸汽压力的较小偏差可以在再沸器温度和再沸器热占状中产生相当大的误差。此外,如果从不准确的关键常数估计蒸汽压力,误差也会更大。再沸器温度观察到高达13%的偏差,可用于再沸器的热量占REGOILER温度,高达16%。结果表明,可靠的模拟和工艺设计强烈依赖于酯的所选物理性质,特殊的蒸气压,这些物理性质从可用的实验数据和使用组贡献和相应的状态模型产生。

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