基于N2与CH4分离的低浓度煤层气两级浓缩技术

    Two Stage Concentration Technology for Low Concentration Coal-bed Mathane Based on Separation Between Methane and Nitrogen

    • 摘要: N2与CH4分子直径相近,两者分离技术是困扰低浓度煤层气浓缩工艺发展的技术难题之一。采用两级变压吸附技术分离提纯低浓度煤层气中的N2与CH4,选取氮烷分离专用碳分子筛,集成创新碳分子筛充填工艺,同时为平衡分离性能与工艺成本间关系,将相同结构设计与碳分子筛的不同混合比例设计相结合,最终完成煤层气中氮烷分离技术工艺设计。现场实践表明,两级变压吸附浓缩技术可将CH4浓度为24%的原料气,逐级浓缩后,渐次从51%提至86%,且CH4回收率超过65%,实现了低浓度煤层气的N2与CH4的分离提纯浓缩目标,为低浓度煤层气的利用创造了技术条件。

       

      Abstract: The molecule diameter of nitrogen and methane is similar and the separation technology is one of the technical problems for the development of low concentration coal-bed gas concentration technology. In this paper, two stage pressure swing adsorption (PSA) was applied for the separation and purification of low concentration coal-bed methane and nitrogen. Selecting special carbon molecular sieve for silazane separation and integrated innovation of carbon molecular sieve filling process, at the same time, to balance the relationship between separation performance and process cost, the same structure design and different mixing proportion design of carbon molecular sieve is combined to finally complete coal-bed mathe silazane separation process design. Field practice shows that two stage pressure swing adsorption concentration technology can enrich CH4 concentration of 24% raw material gas step by step, gradually from 51% to 86% and methane recovery rate of CH4 is more than 65%, which achieves the separation concentration and purification of N2 and CH4 of low concentration coal-bed gas, and creates conditions for the use of low concentration coal-bed gas.

       

    /

    返回文章
    返回