表面活性剂改性强化煤中CH4解吸−扩散动力学机制研究

Kinetic mechanism of surfactant−enhanced CH4 desorption and diffusion in coal

  • 摘要: 为了探究表面活性剂改性对煤中甲烷(CH4)动力学特性的影响,以淮北许曈33采区的烟煤为主要研究对象,选取十二烷基三甲基溴化铵(DTAB)、烷基糖苷(APG)、甲基三甲氧基硅烷(MTMS)、十二烷基硫酸钠(SDS)、聚环氧乙烷(PEO) 5种不同类型表面活性剂处理煤样,测试其在常压条件下CH4的解吸特性,并基于单孔扩散模型和时变扩散模型拟合获得扩散系数;通过气体(N2或CO2)吸附法、傅里叶红外光谱(FT−IR)表征研究了不同类型表面活性剂处理前后煤样微观孔隙和化学结构的变化规律;基于元素分析(EA)、13C固体核磁共振光谱(13C−NMR)和X射线光电子能谱(XPS)数据构建了煤样改性前后的2种大分子结构模型,利用分子动力学(MD)模拟研究了煤样微观化学结构变化对CH4吸附动力学特性的影响。结果表明:5种表面活性剂改性对煤体的微孔结构影响显著,其中与MC煤样相比,MC-PEO样品的微孔比表面积下降30%,微孔孔体积降低25.6%;基于FT−IR分峰拟合结果,MC-PEO煤样的亚甲基/甲基(CH2/CH3)基团峰面积比值从MC的0.31增至0.39,羧基和羰基等极性基团峰面积相对百分比从MC的18.1%降至16.9%,而其余4种表面活性剂处理后煤体的表面性质变化与MC-PEO相反。其次,在0.74~2.0 MPa不同吸附平衡压力下,MC-PEO煤样中CH4解吸量增加7.0%~24.1%,扩散系数提高3%~19.8%。构建的MC和MC-PEO煤分子结构模型的化学分子式分别为C185H132O15N3和C185H141O13N3,基于MD模拟的理论扩散系数从0.3×10−9 m2/s(MC)增至1.2×10−9 m2/s(MC-PEO),与实验结果趋势相一致。该研究成果在宏观和微观层面上协同揭示了非离子表面活性剂PEO通过降低烟煤中微孔吸附位点和表面极性基团的数量增强CH4解吸−扩散过程的作用机制,可为提高瓦斯抽采效率提供一定的理论依据。

     

    Abstract: The impact of surfactant modification on the kinetic properties of methane (CH4) in coal is examined, with Xutong coal samples taken as the primary research object. Five surfactants — dodecyltrimethylammonium bromide (DTAB), alkyl polyglucoside (APG), methyltrimethoxysilane (MTMS), sodium dodecyl sulfate (SDS), and polyethylene oxide (PEO) — were employed to treat the coal samples. The performance of CH4 desorption under varying pressure settings was evaluated, and diffusion coefficients were obtained based on fitting single pore diffusion models and time-varying diffusion models. The alterations in the microscopic pore architecture and oxygenated functional groups of coal samples pre- and post-surfactant treatment were analyzed using gas (N2 or CO2) adsorption and Fourier-transform infrared spectroscopy (FT−IR). Macromolecular structural models of the coal samples were created before to and during modification, based on elemental analysis, 13C nuclear magnetic resonance (13C−NMR) spectroscopy, and X-ray photoelectron spectroscopy (XPS) data. Molecular dynamics (MD) simulations were utilized to investigate the impact of tiny chemical structural alterations on the kinetic characteristics of CH4. Results show that all five surfactants significantly altered the micropore structure of the coal. Relative to the unmodified MC sample, the MC-PEO sample exhibited a 30% decrease in micropore-specific surface area and a 25.6% reduction in micropore volume. FT−IR analysis revealed that the CH2/CH3 ratio of the MC-PEO sample increased from 0.31 to 0.39, while the proportion of polar functional groups (e.g., carboxyl and carbonyl) decreased from 18.1% to 16.9%. In contrast to MC-PEO, treatments with the other four surfactants induced opposite changes in the surface properties of coal. Under adsorption equilibrium pressures ranging from 0.74 to 2.0 MPa, CH4 desorption from MC-PEO increased by 7.0%−24.1%, with the diffusion coefficient rising by 3.0%−19.8%. The chemical formulas of the molecular models for MC and MC-PEO coal were determined to be C185H132O15N3 and C185H141O13N3, respectively. MD simulation results indicated that the theoretical diffusion coefficient increased from 0.3×10−9 m2/s (MC) to 1.2×10−9 m2/s (MC-PEO), consistent with the experimental trend. Collectively, these findings reveal at both macroscopic and microscopic levels that the nonionic surfactant PEO promotes CH4 desorption and diffusion by reducing micropore adsorption sites and the number of surface polar oxygen-containing groups in bituminous coal. A theoretical basis for improving coalbed methane extraction efficiency is provided.

     

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