乙二醇表面改性钼镍双金属型加氢催化剂的制备及性能OA
Preparation and performance of ethylene glycol surface-modified molybdenum-nickel bimetallic hydrogenation catalysts
以乙二醇为助剂,采用 N2 吸附-脱附,NH3-TPD,H2-TPR,TEM,XPS 等方法研究了助剂表面改性对 Mo-Ni 双金属型加氢催化剂性质及性能的影响.实验结果表明,与无添加助剂的催化剂相比,助剂使催化剂的MoS2 分散度由 0.278 提升至 0.317~0.341,提高 Mo 物种硫化程度,促进硫化过程中 Mo6+经 Mo5+向 Mo4+转化,较低助剂用量可显著提高硫化后催化剂中 Mo4+占比.助剂还可显著降低 Ni2+占比,促进 Ni2+向 NiMoS 活性相转化.在反应压力 6.0 MPa、反应温度 340℃、体积空速1.5 h-1、氢油体积比500的条件下,随着助剂用量增加,催化剂芳烃饱和性能先升高后降低;助剂用量为12.5%(φ)的催化剂加氢产物中饱和烃增幅最大,相比原料增加 11.7 百分点.
By using ethylene glycol as a promoter,N2 adsorption-desorption,NH3-TPD,H2-TPR,TEM,and XPS were employed to explore the influence of promoters on the structure and hydrogenation performance of Mo-Ni bimetallic hydrogenation catalysts.The experimental results show that compared to catalysts without promoters,the MoS2 dispersion degree of catalysts with promoters increases from 0.278 to 0.317-0.341,and the promoters enhance the sulfidation degree of Mo species.Additionally,promoters facilitate the transformation of Mo6+to Mo4+via Mo5+during sulfidation,with low promoter dosage significantly increasing the proportion of Mo4+in the sulfided catalysts.The promoters also markedly reduce the proportion of Ni2+and promoted the conversion of Ni2+to the NiMoS active phase.Under the conditions of 6.0 MPa,340℃,volume space velocity of 1.5 h-1,and a hydrogen/oil volume ratio of 500,the aromatic saturation performance of the catalysts initially increased and then decrease with increasing promoter dosage.The catalyst with 12.5%(φ)promoter dosage exhibits the highest increase in saturated hydrocarbon content in the hydrogenation products,with an increase of 11.7 percentage points relative to the feedstock.
穆福军;李雪婧;隋宝宽;刘文洁;袁胜华;耿新国
中石化(大连)石油化工研究院有限公司,辽宁 大连 116045中石化(大连)石油化工研究院有限公司,辽宁 大连 116045中石化(大连)石油化工研究院有限公司,辽宁 大连 116045中石化(大连)石油化工研究院有限公司,辽宁 大连 116045中石化(大连)石油化工研究院有限公司,辽宁 大连 116045中石化(大连)石油化工研究院有限公司,辽宁 大连 116045
化学化工
助剂表面改性加氢催化剂活性相化学态
promotersurface modificationhydrogenation catalystactive phasechemical state
《石油化工》 2026 (6)
829-837,9
中国石油化工股份有限公司项目(124027)中石化(大连)石油化工研究院有限公司项目(DLYZL2024052310).
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