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深部煤炭地下气化过程中焦油析出特性

Tar precipitation characteristics during deep underground coal gasification

  • 摘要: 煤炭地下气化技术是未来煤炭清洁高效利用的发展方向,有望成为我国深部煤炭开采和利用的重要补充。而煤炭地下气化过程中产生的高温煤气携带有机污染物对地下水造成的潜在污染风险,成为限制该技术工业化应用的瓶颈问题。针对深部煤炭地下气化干馏干燥带高温高压环境下煤焦油析出机制尚不明确的问题,本研究采用煤炭加压热解实验装置,结合气相色谱-质谱联用技术(GC-MS),明晰了热解产物分布特征与焦油化学组分演化规律,揭示了深部煤炭地下气化过程中煤焦油的多阶段析出机制。结果表明,3 MPa压力条件下,随着热解温度升高,半焦产率持续下降,焦油与煤气产率显著上升,其中500 ℃时煤气产率较400 ℃提高4.3倍,是产气效率提升的核心温度区间;焦油的化学组成随热解温度升高呈现显著的阶段性转变特征。400~500 ℃时脂肪烃为绝对主导组分,占比分别达73.65%和71.6%。600 ℃时多环芳烃取代脂肪烃成为主要组分,其占比从400~500 ℃的1.25%和4.21%升至48.67%,700 ℃时非烃化合物成为焦油的核心成分,占比达到32.32%。热解压力对焦油族组分演化具有显著调控作用,700 ℃常压热解条件下,煤焦中沥青质相对质量分数达到峰值;随着热解压力升高,沥青质相对质量分数持续减少,饱和烃相对质量分数逐步升高,当压力大于2 MPa时,饱和烃已完全释放,而芳香烃、胶质和沥青质的产率仍随压力升高持续增大。本研究揭示了加压热解煤焦油的析出规律,为深部煤炭地下气化过程中污染物控制与工艺优化提供了理论依据。

     

    Abstract: Underground coal gasification represents a promising direction for the clean and efficient utilization of coal in the future and is expected to serve as a significant supplement to deep coal mining and utilization in China. However, the potential risk of groundwater contamination posed by organic pollutants carried by high-temperature syngas generated during UCG has emerged as a bottleneck constraining the industrial application of this technology. Addressing the unclear mechanism of coal tar formation under the high-temperature and high-pressure conditions in the drying and pyrolysis zone during deep UCG, this study employs a pressurized coal pyrolysis experimental apparatus combined with gas chromatography-mass spectrometry (GC-MS) to elucidate the distribution characteristics of pyrolysis products and the evolutionary patterns of tar chemical components, revealing the multi-stage formation mechanism of coal tar during deep UCG. The results indicate that under a pressure of 3 MPa, as the pyrolysis temperature increases, the char yield continuously decreases, while the yields of tar and syngas significantly increase. Specifically, at 500 °C, the syngas yield is 4.3 times higher than that at 400 °C, identifying this range as a critical temperature interval for enhancing gas production efficiency. The chemical composition of tar exhibits pronounced stage-wise transformation characteristics with increasing pyrolysis temperature. In the range of 400–500 °C, aliphatic hydrocarbons dominate the composition, accounting for 73.65% and 71.6%, respectively. At 600 °C, polycyclic aromatic hydrocarbons replace aliphatic hydrocarbons as the main component, with their proportion increasing from 1.25% and 4.21% at 400–500 °C to 48.67%. At 700 °C, non-hydrocarbon compounds become the core components of tar, accounting for 32.32%. Pyrolysis pressure significantly regulates the evolution of tar group components. Under atmospheric pressure pyrolysis conditions at 700 °C, the asphaltene content in coal tar peaks. As the pyrolysis pressure increases, the relative content of asphaltenes gradually decreases, while the relative content of saturated hydrocarbons gradually increases. When the pressure exceeds 2 MPa, saturated hydrocarbons are completely released, whereas the yields of aromatics, resins, and asphaltenes continue to increase with rising pressure. This study reveals the formation law of coal tar during pressurized pyrolysis, providing a theoretical basis for pollutant control and process optimization in deep UCG.

     

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