基于巨正则蒙特卡罗和分子动力学方法的多元气体在气肥煤中的竞争吸附研究OA
Study on competitive adsorption of multicomponent gas in gas-fat coal based on GCMC and molecular dynamics
为探究 CH4、CO2、H2S 3 种气体在气肥煤中的赋存特性,揭示不同温度下 3 种气体在气肥煤中的吸附动力学过程及不同体积分数下 3 种气体的竞争吸附微观机理,基于巨正则蒙特卡罗(GCMC)和分子动力学(MD)方法,研究温度为 273.15~313.15 K、压力为 0~3 MPa 条件下,CH4、CO2 和 H2S 在煤层中的二元混合组分(CH4/H2S 和 CO2/H2S)的竞争吸附,以及不同体积分数对气体吸附量、等量吸附热、能量分布、选择性系数和概率密度分布的影响.结果表明:煤对气体的吸附量由大到小依次为 H2S、CO2、CH4;CH4、CO2 和 H2S 的吸附动力学特性与准二级动力学模型吻合良好,拟合度均值分别为 0.993 0、0.999 7、0.999 8;吸附平衡时,吸附量随温度的升高而逐渐降低,二级吸附速率常数随温度升高而先增大后减小;当 CH4 的体积分数由 10%增至90%时,CH4 的饱和吸附量由 1.86 cm3/g 增至 7.89 cm3/g,H2S 的饱和吸附量由 41.54 cm3/g 降至28.71 cm3/g;CO2 的体积分数由 10%增至 90%时,CO2 的饱和吸附量由 6.64 cm3/g 增至 26.66 cm3/g,H2S 的饱和吸附量由 36.17 cm3/g 降至 10.86 cm3/g;CH4/H2S 和 CO2/H2S 二元组分的吸附选择性系数均随平衡压力的增大呈指数形式衰减,即先快速减小后缓慢减小,最终趋于平缓.
To investigate the occurrence characteristics of CH4,CO2,and H2S in gas-fat coal,reveal their adsorption kinetic pro-cesses in gas-fat coal at different temperatures and the microscopic mechanism of competitive adsorption among the three gases un-der different volume fractions,the competitive adsorption of binary mixtures(CH4/H2S and CO2/H2S)in coal seams was studied us-ing Grand Canonical Monte Carlo(GCMC)and molecular dynamics(MD)methods under conditions of 273.15-313.15 K and 0-3 MPa.The influences of volume fractions on gas adsorption capacity,isosteric heat of adsorption,energy distribution,selectivity coef-ficient,and probability density distribution were analyzed.The results show that the order of gas adsorption capacity in coal from high to low is H2S>CO2>CH4.The adsorption kinetics of CH4,CO2,and H2S agree well with the pseudo-second-order kinetic mod-el,with average fitting degrees of 0.993 0,0.999 7,and 0.999 8,respectively.At adsorption equilibrium,the adsorption capacity gradually decreases with increasing temperature,while the second-order adsorption rate constant k2 first decreases and then increases with rising temperature.When the volume fraction of CH4 increases from 10%to 90%,the saturated adsorption capacity of CH4 rises from 1.86 cm3/g to 7.89 cm3/g,while that of H2S decreases from 41.54 cm3/g to 28.71 cm3/g.As the volume fraction of CO2 in-creases from 10%to 90%,the saturated adsorption capacity of CO2 increases from 6.64 cm3/g to 26.66 cm3/g,whereas that of H2S decreases from 36.17 cm3/g to 10.86 cm3/g.The adsorption selectivity coefficients of the CH4/H2S and CO2/H2S binary systems de-cay exponentially with increasing equilibrium pressure:they decrease rapidly at first,then slowly,and finally tend to be stable.
张庆锋;王长禄;郑义;邢迎欢
国能神东煤炭集团 布尔台煤矿,内蒙古 鄂尔多斯 017200煤科通安(北京)智控科技有限公司,北京 100013||煤炭科学技术研究院有限公司,北京 100013||北京市煤矿安全工程技术研究中心,北京 100013||煤炭智能开采与岩层控制全国重点实验室,北京 100013煤科通安(北京)智控科技有限公司,北京 100013||煤炭科学技术研究院有限公司,北京 100013||北京市煤矿安全工程技术研究中心,北京 100013||煤炭智能开采与岩层控制全国重点实验室,北京 100013辽宁工程技术大学 安全科学与工程学院,辽宁 阜新 123000
矿业与冶金
巨正则蒙特卡罗分子动力学多元气体竞争吸附吸附动力学
Grand Canonical Monte Carlo(GCMC)molecular dynamics(MD)multicomponent gascompetitive adsorptionad-sorption kinetics
《煤矿安全》 2026 (6)
36-48,13
国家自然科学基金资助项目(52174183)辽宁省自然科学基金资助项目(2024-BS-257)
评论