In order to remove N_(2) from low quality natural gas,a mathematical model has been established by Aspen adsorption,using the CH_(4)-selective sorbent silicalite-1 pellets.The dynamic adsorption isotherm was first sim...In order to remove N_(2) from low quality natural gas,a mathematical model has been established by Aspen adsorption,using the CH_(4)-selective sorbent silicalite-1 pellets.The dynamic adsorption isotherm was first simulated by breakthrough simulation of a CH_(4)/N_(2) mixture at different adsorption pressures and feed flow rates based on breakthrough experiments.The resulting simulated CH_(4) dynamic adsorption amounts were very close to the experimental data at three different adsorption pressures(100,200,and 300 kPa).Moreover,a single-bed,three-step pressure swing adsorption(PSA)experiment was performed,and the results were in good agreement with the simulated data,further corroborating the accuracy of the gas dynamic adsorption isotherm obtained by the simulation method.Finally,based on the simulated dynamic adsorption isotherm of CH_(4) and N_(2),a four-bed,eight-step PSA process has been designed,which enriched 75%(vol)CH_(4) and 80%(vol)CH_(4) to 95%(vol)and 99%(vol),and provided 99%(vol)recovery.展开更多
1,1,1,3,3-五氟丙烷-氟化氢混合物是一种二元最低共沸物。在计算机模拟和分析的基础上,研究了变压精馏分离五氟丙烷-氟化氢的工艺流程。选用Aspen P lus软件内置的热力学模型W ILS-HF描述五氟丙烷-氟化氢二元共沸体系的气液平衡。根据...1,1,1,3,3-五氟丙烷-氟化氢混合物是一种二元最低共沸物。在计算机模拟和分析的基础上,研究了变压精馏分离五氟丙烷-氟化氢的工艺流程。选用Aspen P lus软件内置的热力学模型W ILS-HF描述五氟丙烷-氟化氢二元共沸体系的气液平衡。根据实验数据,回归该热力学模型中的交互作用参数,模型的计算结果与实际数据吻合较好。使用Aspen P lus对整个分离流程进行模拟计算,以系统能耗最低为目标,对重要的工艺参数进行了优化,模拟结果对工业过程的设计具有一定的指导意义。展开更多
乙醇苯混合物是一种二元最低共沸液体混合物。研究了变压精馏分离乙醇苯工艺流程,以W ilson活度系数方程作为物性计算方法,使用过程模拟软件Aspen P lus对整个分离流程进行模拟计算,以系统能耗最低为目标,对重要的工艺参数进行了优化,...乙醇苯混合物是一种二元最低共沸液体混合物。研究了变压精馏分离乙醇苯工艺流程,以W ilson活度系数方程作为物性计算方法,使用过程模拟软件Aspen P lus对整个分离流程进行模拟计算,以系统能耗最低为目标,对重要的工艺参数进行了优化,提出的工艺方案可为工艺装置设计提供理论参考。展开更多
文摘In order to remove N_(2) from low quality natural gas,a mathematical model has been established by Aspen adsorption,using the CH_(4)-selective sorbent silicalite-1 pellets.The dynamic adsorption isotherm was first simulated by breakthrough simulation of a CH_(4)/N_(2) mixture at different adsorption pressures and feed flow rates based on breakthrough experiments.The resulting simulated CH_(4) dynamic adsorption amounts were very close to the experimental data at three different adsorption pressures(100,200,and 300 kPa).Moreover,a single-bed,three-step pressure swing adsorption(PSA)experiment was performed,and the results were in good agreement with the simulated data,further corroborating the accuracy of the gas dynamic adsorption isotherm obtained by the simulation method.Finally,based on the simulated dynamic adsorption isotherm of CH_(4) and N_(2),a four-bed,eight-step PSA process has been designed,which enriched 75%(vol)CH_(4) and 80%(vol)CH_(4) to 95%(vol)and 99%(vol),and provided 99%(vol)recovery.
文摘1,1,1,3,3-五氟丙烷-氟化氢混合物是一种二元最低共沸物。在计算机模拟和分析的基础上,研究了变压精馏分离五氟丙烷-氟化氢的工艺流程。选用Aspen P lus软件内置的热力学模型W ILS-HF描述五氟丙烷-氟化氢二元共沸体系的气液平衡。根据实验数据,回归该热力学模型中的交互作用参数,模型的计算结果与实际数据吻合较好。使用Aspen P lus对整个分离流程进行模拟计算,以系统能耗最低为目标,对重要的工艺参数进行了优化,模拟结果对工业过程的设计具有一定的指导意义。
