Samples of methane molecules grade diameter channel CHA-type molecular sieves(Chabazite-K, SAPO-34 and SSZ-13) were investigated using the adsorption separation of CH4/N2 mixtures. The isotherms recorded for CH4 and N...Samples of methane molecules grade diameter channel CHA-type molecular sieves(Chabazite-K, SAPO-34 and SSZ-13) were investigated using the adsorption separation of CH4/N2 mixtures. The isotherms recorded for CH4 and N2 follow a typical type-Ι behavior, which were fitted well with the Sips model(R2>0.999) and the selectivity was calculated using IAST theory. The results reveal that Chabazite-K has the highest selectivity(SCH4/N= 5.5).2 SSZ-13 has the largest capacity, which can adsorb up to a maximum of 30.957 cm3·g-1(STP) of CH4, due to it having the largest pore volume and surface area, but the lowest selectivity(SCH4/N2= 2.5). From the breakthrough test, we can conclude that SSZ-13 may be a suitable candidate for the recovery of CH4 from low concentration methane(CH4<20%) based on its larger pore volume and higher CH4 capacity. Chabazite-K is more suited to the separation of high concentration methane(CH4>50%) due to its higher selectivity.展开更多
为给煤层气中甲烷与氮气的变压吸附分离提供相关的模型和热力学数据,采用静态体积法测试了温度298.15、313.15、328.15 K时,CH4/N2在自制炭分子筛上的吸附量,使用Langmuir等9个吸附模型对吸附量进行了非线性拟合,通过比较各吸附模型的...为给煤层气中甲烷与氮气的变压吸附分离提供相关的模型和热力学数据,采用静态体积法测试了温度298.15、313.15、328.15 K时,CH4/N2在自制炭分子筛上的吸附量,使用Langmuir等9个吸附模型对吸附量进行了非线性拟合,通过比较各吸附模型的拟合精度,得出最优化体积填充模型DA拟合效果最好,经验方程Freundlich模型拟合效果最差,Langmuir、Sips和Toth等模型拟合效果适中,同种模型对于N_2的拟合程度好于CH_4。同时对各模型的拟合参数进行了分析,BET方程不适合描述CH_4、N_2在该炭分子筛上的吸附,Langmuir、Toth、E-L等模型中饱和吸附量qm均随温度的升高而减小,且温度变化对于N_2的饱和吸附量影响较大;E-L模型、Toth模型和Sips模型中反映吸附剂表面能量不均匀性的参数n随着温度的升高而增大,F-L模型中分形维数D的增大表明温度升高增加了炭分子筛表面不均一性。吸附热力学分析表明,该炭分子筛对于CH_4、N_2的平均等量吸附热分别为11.80、9.06 k J/mol,均属于物理吸附;随着吸附量的增大,N_2的等量吸附热变化范围大于CH_4。展开更多
基金financial support from the National Natural Science Foundation of China (Nos. 51672186, 21676175)
文摘Samples of methane molecules grade diameter channel CHA-type molecular sieves(Chabazite-K, SAPO-34 and SSZ-13) were investigated using the adsorption separation of CH4/N2 mixtures. The isotherms recorded for CH4 and N2 follow a typical type-Ι behavior, which were fitted well with the Sips model(R2>0.999) and the selectivity was calculated using IAST theory. The results reveal that Chabazite-K has the highest selectivity(SCH4/N= 5.5).2 SSZ-13 has the largest capacity, which can adsorb up to a maximum of 30.957 cm3·g-1(STP) of CH4, due to it having the largest pore volume and surface area, but the lowest selectivity(SCH4/N2= 2.5). From the breakthrough test, we can conclude that SSZ-13 may be a suitable candidate for the recovery of CH4 from low concentration methane(CH4<20%) based on its larger pore volume and higher CH4 capacity. Chabazite-K is more suited to the separation of high concentration methane(CH4>50%) due to its higher selectivity.
文摘为给煤层气中甲烷与氮气的变压吸附分离提供相关的模型和热力学数据,采用静态体积法测试了温度298.15、313.15、328.15 K时,CH4/N2在自制炭分子筛上的吸附量,使用Langmuir等9个吸附模型对吸附量进行了非线性拟合,通过比较各吸附模型的拟合精度,得出最优化体积填充模型DA拟合效果最好,经验方程Freundlich模型拟合效果最差,Langmuir、Sips和Toth等模型拟合效果适中,同种模型对于N_2的拟合程度好于CH_4。同时对各模型的拟合参数进行了分析,BET方程不适合描述CH_4、N_2在该炭分子筛上的吸附,Langmuir、Toth、E-L等模型中饱和吸附量qm均随温度的升高而减小,且温度变化对于N_2的饱和吸附量影响较大;E-L模型、Toth模型和Sips模型中反映吸附剂表面能量不均匀性的参数n随着温度的升高而增大,F-L模型中分形维数D的增大表明温度升高增加了炭分子筛表面不均一性。吸附热力学分析表明,该炭分子筛对于CH_4、N_2的平均等量吸附热分别为11.80、9.06 k J/mol,均属于物理吸附;随着吸附量的增大,N_2的等量吸附热变化范围大于CH_4。
