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Preparation of hierarchical HZSM-5 based sulfated zirconium solid acid catalyst for catalytic upgrading of pyrolysis vapors from lignite pyrolysis

机译:制备基于HZSM-5的分级硫酸锆固体酸催化剂,用于褐煤热解催化热解蒸气的提质

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H5 was developed to mesoporous system via alkali treatment, and sulfated zirconia (SZr) modified hierarchical HZSM-5 (AT(0.2)/H5) catalysts (named AT(0.2)/SZxH5) were successfully prepared by a series of post-treated method followed by Zr(NO3)(4)center dot 5H(2)O and H2SO4 as active component. The innovative approach really enhanced acidity of AT(0.2)/H5 support, which results from the interaction of the sulfate groups attached to zirconia that doped on MFI framework with silanol groups. Adding active component can not only compensate for the loss of acid sites caused by NaOH treatment, but also re-develop more active sites owing to the formation of SZr. Meanwhile, NH3-TPD showed higher strong acid sites and weak acid sites in AT(0.2)/SZ(6.1 )H5 than other prepared catalysts. The catalytic activity in converting lignite pyrolysis volatiles to light aromatics, including benzene, toluene, ethylbenzene, xylene and naphthalene (BTEXN), correlates well with the enhanced acidity. Compared with H5, the yield of light aromatics increased significantly from 15.2 to 19.3 mg/g over AT(0.2)/SZ(6.1) H5 at 600 degrees C. According to the characterization of N-2 adsorption-desorption, SEM, and XRD, both the S species as SO42- and Z species as ZrO2 improved the textural properties of the support itself. Besides, the molar ratio of S/Zr was in direct proportion to the yield of BTEXN in a certain range, and 6:1 exhibited the optimal catalytic performance. The prepared solid acid catalyst provides a promising strategy to directional prepare light aromatics during lignite catalytic pyrolysis.
机译:通过碱处理将H5开发为介孔体系,并通过一系列后处理方法成功制备了硫酸化氧化锆(SZr)改性的分级HZSM-5(AT(0.2)/ H5)催化剂(命名为AT(0.2)/ SZxH5)。其次是Zr(NO3)(4)中心点5H(2)O和H2SO4作为活性成分。该创新方法确实增强了AT(0.2)/ H5载体的酸度,这是由于MFI骨架上掺杂的氧化锆上附着的硫酸盐基团与硅烷醇基团之间的相互作用所致。添加活性组分不仅可以补偿由于NaOH处理引起的酸位损失,而且由于SZr的形成还可以重新形成更多的活性位。同时,NH3-TPD在AT(0.2)/ SZ(6.1)H5中显示出比其他制备的催化剂更高的强酸中心和弱酸中心。将褐煤热解挥发物转化为轻质芳烃(包括苯,甲苯,乙苯,二甲苯和萘(BTEXN))的催化活性与提高的酸度密切相关。与H5相比,在600摄氏度时,相对于AT(0.2)/ SZ(6.1)H5,轻质芳烃的产率从15.2 mg / g显着增加。根据N-2吸附-解吸,SEM和XRD的表征,无论是作为SO42-的S物种还是作为ZrO2的Z物种都改善了载体本身的质构性质。另外,在一定范围内,S / Zr的摩尔比与BTEXN的收率成正比,最佳的催化性能为6∶1。制备的固体酸催化剂为褐煤催化热解过程中定向制备轻质芳烃提供了有希望的策略。

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