Preparation of core-shell structural twin HZSM-5@Silicalite-1 catalysts and its performance for toluene alkylation with methanol
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摘要: 本研究采用水热结晶法合成了孪晶HZSM-5分子筛,并在表面外延生长Silicalite-1(S-1)纯硅沸石,制备了HZSM-5@Silicalite-1核壳结构催化剂。与孪晶HZSM-5相比,HZSM-5@Silicalite-1核壳结构催化剂在甲苯甲醇烷基化反应中表现出优异的催化性能。在470 ℃、0.1 MPa和临氢反应条件下,HZSM-5@40Silicalite-1催化剂的甲苯单程转化率为8.5%,对二甲苯选择性为98.4%。进一步研究了核相HZSM-5与S-1壳层前驱体固液质量比对表面S-1晶体生长的影响,同时考察了S-1壳层对孪晶HZSM-5催化性能的影响。通过SEM、XRD、XRF、液体静态吸附、N2吸附-脱附、NH3-TPD、Py-FTIR等表征实验对核壳材料的结构和酸性质进行了详细研究。
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关键词:
- 孪晶HZSM-5 /
- Silicalite-1 /
- 核壳结构 /
- 择形催化 /
- 对二甲苯
Abstract: The technology of alkylation of toluene with methanol to p-xylene has attracted much attention due to the high selectivity of p-xylene and low energy consumption in product separation unit. Twin HZSM-5 molecular sieve has the characteristics of large coverage proportion of zigzag channels on the surface and less aluminum distribution on the outer surface. It shows high selectivity for p-xylene in the alkylation of toluene and methanol. In this paper, silicalite-1 (S-1) was grown epitaxially on the surface of twin HZSM-5 molecular sieve by hydrothermal crystallization, and twin HZSM-5@Silicalite-1 core-shell catalyst was obtained. Compared with twin HZSM-5, HZSM-5@40Silicalite-1 core-shell catalyst shows excellent catalytic performance in toluene methanol alkylation. Under the reaction conditions of 470 ℃, 0.1 MPa and hydrogen atmosphere, the conversion of toluene is 8.5% and the selectivity of p-xylene is 98.4%. Then, the effect of solid-liquid mass ratio of nuclear HZSM-5 and silicalite-1 shell precursors on the growth of silicalite-1 crystal was further studied, and the effect of silicalite-1 on the catalytic performance of twin HZSM-5 was investigated. The pore structure and acid properties of core-shell materials were studied in detail by SEM, XRD, XRF, liquid static adsorption, N2 adsorption desorption, NH3-TPD and Py-FTIR.-
Key words:
- twin HZSM-5 /
- silicalite-1 /
- core-shell structure /
- shape-selective catalysis /
- para-xylene
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表 1 样品的Si/Al物质的量比
Table 1 Molar ratio Si / Al of the samples
Sample Si/Al(mol ratio) HZSM-5 152 HZSM-5@10S-1 171 HZSM-5@20S-1 186 HZSM-5@40S-1 199 表 2 HZSM-5和HZSM-5@S-1分子筛的结构参数
Table 2 Structural properties of HZSM-5 and HZSM-5@S-1 molecular sieves
Sample ${S} _{ {\rm{BET} } }^{\rm{a} } /$(m2·g−1) ${S} _{ {\rm{micro} } }^{\rm{b} } /$(m2·g−1) ${S} _{ {\rm{exter} } }^{\rm{b} } /$(m2·g−1) ${v}_ {\rm{total} } /$(cm3·g−1) $v_{ {\rm{micro} } }^{\rm{b} } /$(cm3·g−1) $v_{ {\rm{meso} } }^{\rm{b} }/$(cm3·g−1) HZSM-5 370 288 82 0.18 0.12 0.06 HZSM-5@10S-1 351 250 101 0.18 0.11 0.07 HZSM-5@20S-1 339 240 99 0.18 0.10 0.08 HZSM-5@40S-1 351 260 91 0.20 0.11 0.09 a Calculated by the BET method; b Calculated using the t-plot method; c Calculated using vtotal −vmicro 表 3 探针分子PX、MX和OX的异构转化率
Table 3 isomerization conversion of probe molecules PX, MX and OX
Sample PX isomerization conversion /% MX isomerization conversion /% OX isomerization conversion /% Black − − − HZSM-5 3.9 1.6 1.5 HZSM-5@10S-1 1.9 0.7 0.9 HZSM-5@20S-1 1.3 0.4 0.6 HZSM-5@40S-1 0.8 0.1 0.5 -
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