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MSE分子筛的孔道调控和酸量对催化裂解正庚烷制低碳烯烃性能的影响
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作者 范军 杨诗棋 +4 位作者 濮鑫 叶磊 朱卡克 纪晔 刘纪昌 《石油学报(石油加工)》 北大核心 2025年第1期1-13,共13页
多级孔化和调控酸量是提高MSE分子筛催化裂解性能的有效途径。通过珠磨-重结晶法合成了具有纳米尺度、窄粒径分布的多级孔UZM-35分子筛,探讨了制备过程中珠磨时间和重结晶时间等因素对分子筛结构的影响,并通过硝酸溶液脱铝降低MSE分子... 多级孔化和调控酸量是提高MSE分子筛催化裂解性能的有效途径。通过珠磨-重结晶法合成了具有纳米尺度、窄粒径分布的多级孔UZM-35分子筛,探讨了制备过程中珠磨时间和重结晶时间等因素对分子筛结构的影响,并通过硝酸溶液脱铝降低MSE分子筛的酸量。采用X-射线衍射(XRD)、扫描电子显微镜(SEM)、氮气物理吸附-脱附、固体核磁、氨气程序升温脱附(NH 3-TPD)和吡啶红外(Py-IR)等手段对分子筛的形貌、孔道结构和酸性质进行表征测定。以正庚烷催化裂解制备低碳烯烃为探针反应,对MSE分子筛进行性能评价,结果表明:通过引入多级孔结构和降低酸量促进MSE孔道中的单分子裂解反应,抑制氢转移副反应,使乙烯+丙烯收率提高,失活速率降低。在反应温度913 K、质量空速5 h-1的条件下,脱铝多级孔UZM-35分子筛的裂化机理比达到73.5,氢转移系数低至0.11;乙烯+丙烯收率为48.6%,比初始UZM-35分子筛提高了6.1%;反应10 h的失活率为4.1%,比初始UZM-35分子筛降低了14.3%。 展开更多
关键词 低碳烯烃 催化裂解 多级孔 UZM-35分子筛 珠磨-重结晶
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Effect of Steam Treatment on the Catalytic Performance of ZSM-5 in the Co-conversion of Methanol and n-Hexane to Aromatics
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作者 Wei Shumei Xu Yarong +2 位作者 Yang Fan zhu kake zhu Xuedong 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS CSCD 2024年第3期73-81,共9页
Steam pretreatment is a widely used method for modifying the acidity and structure of zeolites,thereby enhancing their catalytic properties.This study systematically investigated the effects of steam treatment on ZSM-... Steam pretreatment is a widely used method for modifying the acidity and structure of zeolites,thereby enhancing their catalytic properties.This study systematically investigated the effects of steam treatment on ZSM-5 zeolites at varying treatment temperatures and durations.The structural evolution of the catalysts was monitored using N2 adsorptiondesorption,X-ray diffraction,inductively coupled plasma optical emission spectroscopy,scanning electron microscopy,NH3 temperature-programmed desorption,in situ pyridine infrared spectroscopy,and thermogravimetric analysis.The characterization results revealed that mesopores were introduced into the ZSM-5 zeolite catalysts through dealumination induced using steam treatment at moderate temperatures(400 and 500℃).Moreover,compared with the parent catalyst,the steam-treated catalysts exhibited a lower amount of acid sites and relative crystallinity,while the n(Si)/n(Al)ratio increased.In the co-conversion of methanol and n-hexane in a fixed bed reactor at 400℃and 0.5 MPa(N2 atmosphere),with a weight hourly space velocity of 1 h−1 and a stoichiometric ratio of 1:1(CH3OH to n-hexane),the steam-treated catalysts displayed a prolonged catalyst lifetime.Particularly,the parent zeolite had a lifetime of 96 h,while the catalyst treated at 500℃for 12 h had a lifetime of up to 240 h.Additionally,the steam-treated catalysts maintained stable n-hexane conversion and improved aromatic selectivity.Notably,these treated catalysts exhibited a lower deactivation rate than the parent catalyst,and would be conducive to industrial scale-up production. 展开更多
关键词 steam ZSM-5 zeolites co-conversion AROMATIZATION METHANOL N-HEXANE
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