郭江, 王美君, 申岩峰, 孔娇, 常丽萍, 鲍卫仁, 谢克昌. 煤热解挥发物对炼焦煤塑性体渗透性的调控研究[J]. 燃料化学学报(中英文), 2022, 50(6): 724-734. DOI: 10.1016/S1872-5813(21)60194-9
引用本文: 郭江, 王美君, 申岩峰, 孔娇, 常丽萍, 鲍卫仁, 谢克昌. 煤热解挥发物对炼焦煤塑性体渗透性的调控研究[J]. 燃料化学学报(中英文), 2022, 50(6): 724-734. DOI: 10.1016/S1872-5813(21)60194-9
GUO Jiang, WANG Mei-jun, SHEN Yan-feng, KONG Jiao, CHANG Li-ping, BAO Wei-ren, XIE Ke-chang. Regulation of permeability of plastic layer of coking coal by volatiles from coal pyrolysis[J]. Journal of Fuel Chemistry and Technology, 2022, 50(6): 724-734. DOI: 10.1016/S1872-5813(21)60194-9
Citation: GUO Jiang, WANG Mei-jun, SHEN Yan-feng, KONG Jiao, CHANG Li-ping, BAO Wei-ren, XIE Ke-chang. Regulation of permeability of plastic layer of coking coal by volatiles from coal pyrolysis[J]. Journal of Fuel Chemistry and Technology, 2022, 50(6): 724-734. DOI: 10.1016/S1872-5813(21)60194-9

煤热解挥发物对炼焦煤塑性体渗透性的调控研究

Regulation of permeability of plastic layer of coking coal by volatiles from coal pyrolysis

  • 摘要: 本研究以低挥发分烟煤C1和高挥发分烟煤C2为研究对象(以下煤样简称为C1和C2),引入褐煤L1和C2在两个温度下热解脱除部分挥发物的半焦作为对照,设计单种煤、混合煤/半焦和分层渗透性实验,结合热重和基式流动度分析,揭示了炼焦煤塑性体渗透性受挥发物释放行为的影响。研究结果表明,低挥发分烟煤C1存在塑性体低渗透性平台期,高挥发分烟煤C2塑性体的渗透性达到最低值后迅速改善,挥发物传质驱动力和阻力的差异导致了两种煤塑性体渗透性的差异;C2会增强挥发物的传质驱动力且热解后半焦颗粒成为塑性体惰性组分,同时也提供部分可转移氢,既改善塑性体渗透性又不破坏其稳定性;软化温度前C2释放的富氢挥发物促进C1塑性体低渗透性的形成并达到最大值;热塑性温区内C2释放的挥发物帮助维持C1塑性体的低渗透性平台期;延长C2挥发物反应消耗部分富氢挥发物,有利于改善C1塑性体的渗透性。

     

    Abstract: The low permeability of plastic layer of coking coal causes the formation of coking pressure, and the evolution of permeability is closely related to the release behavior of volatiles. In this paper, a low-volatile bituminous coal C1 and a high-volatile bituminous coal C2 were selected as research objectives, and a lignite L1 and two semi-cokes produced from the pyrolysis of C2 at two temperatures were used as the contrast. The permeability tests of single coal, binary coal or semi-coke and separated combination were conducted. The influence of volatiles release behaviors on the evolution of permeability of plastic layer was revealed by thermogravimetric and fluidity analyses. The results showed that there was a low permeability plateau stage of plastic layer of C1, while the permeability of plastic layer of C2 was rapidly improved after reaching the lowest. This was related to the difference in the mass transfer conditions of volatiles from two coals. C2 could enhance the mass transfer driving force of volatiles and bring both inert components (semi-coke after pyrolysis) and transferable hydrogen, thus the permeability of plastic layer could be improved without destroying the stability of plastic layer. The hydrogen-rich volatiles released from C2 before its initial softening temperature helped the low permeability of the plastic layer of C1 be formed and reach the maximum. The volatiles released during the plastic stage of C2 helped maintain the low permeability plateau of plastic layer of C1. It was plausible to further improve the permeability of plastic layer of C1 by consuming part of hydrogen-rich volatiles from C2 with prolonging the volatiles’ reaction. This paper provided a new insight in selecting high-volatile coals for improving permeability of the plastic layer from the aspect of volatiles’ release behaviors.

     

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