辉钼矿复合催化剂对哈密煤温和液化性能的影响及活性相变迁规律研究OA
Effects of molybdenite-based composite catalysts on mild liquefaction performance of Hami coal and transformation behavior of active phases
温和条件,尤其是低反应压力下的煤直接液化,可有效降低投资和运行成本.易于获取且具有良好加氢性能的催化剂,对于实现温和条件下煤直接液化的工业化应用至关重要.采用机械活化方法对辉钼矿进行超细化加工,制备不同粒径的MoS2 分散液,并耦合γ-FeOOH制备复合催化剂.通过SEM、XRD和XPS表征,考察了机械活化时间对催化剂组成和分散性的影响.结果表明:延长机械活化时间有利于辉钼矿中活性组分MoS2暴露于矿物表面,同时提高了其在催化剂中的分散性.利用高压釜试验平台,在反应温度450℃、最大压力不超过10 MPa的温和条件下对哈密煤进行直接液化试验.反应过程中,复合催化剂中的 MoS2 保持稳定,而 γ-FeOOH 在300℃时转化为约100 nm的Fe1-xS颗粒.升温过程中Fe1-xS的XRD特征峰向小角度偏移,颗粒尺寸增大,至450℃后保持稳定.与铁基催化剂相比,复合催化剂在450℃恒温30 min~60 min内对沥青质的加氢效果显著,最大油产率达50.64%,提升了6.86%.
Direct coal liquefaction under mild conditions,particularly at low reaction pressures,can effectively reduce both investment and operational costs.The availability of readily available catalysts with good hydrogenation performance is crucial for achieving the industrial application of direct coal liquefaction under mild conditions.Molybdenite was subjected to ultra-fine processing via mechanical activation to prepare MoS2 dispersions with varying particle sizes,which were then compounded with γ-FeOOH to fabricate a composite catalyst.The effects of mechanical activation time on the composition and dispersion of the catalyst were investigated using SEM,XRD and XPS characterization.The results indicate that extending the mechanical activation time facilitates the exposure of MoS2,the active component of molybdenite,on the mineral surface,while improving its dispersion within the catalyst.Utilizing a high-pressure autoclave test platform,direct liquefaction experiments were conducted on Hami coal under mild conditions with a reaction temperature of 450℃and a maximum pressure not exceeding 10 MPa.During the reaction process,the MoS2 in the composite catalyst remained stable,while γ-FeOOH transformed into Fe1-xS particles approximately 100 nm in size at 300℃.The XRD characteristic peaks of Fe1-xS shifted to lower angles during the heating process,accompanied by an increase in particle size,which stabilized after reaching 450℃.Compared with the iron-based catalyst,the composite catalyst demonstrated significant hydrogenation effects on asphaltenes during the 30 min‒60 min isothermal period at 450℃,achieving a maximum oil yield of 50.64%—an increase of 6.86%over that of the iron-based catalyst.
王熺乾;王光耀;赵渊
煤炭科学技术研究院有限公司,100013 北京||国家能源煤炭高效利用与节能减排技术装备重点实验室,100013 北京||中国煤科低碳技术研究院,100013 北京煤炭科学技术研究院有限公司,100013 北京||国家能源煤炭高效利用与节能减排技术装备重点实验室,100013 北京||中国煤科低碳技术研究院,100013 北京煤炭科学技术研究院有限公司,100013 北京||国家能源煤炭高效利用与节能减排技术装备重点实验室,100013 北京||中国煤科低碳技术研究院,100013 北京
化学化工
温和液化复合催化剂活性相变迁哈密煤辉钼矿机械活化液化性能
mild liquefactioncomposite catalystactive phase transformationHami coalmolybdenitemechanical activationliquefaction performance
《煤炭转化》 2026 (3)
37-47,11
国家重点研发计划课题(2023YFB4103402)
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