Synthesis of ZSM-22/SAPO-11 composite molecular sieve-based catalysts with small crystallites and superior n-alkane hydroisomerization performance

To improve oil quality,ZSM-22/SAPO-11 composite molecular sieves were synthesized by adding ZSM-22 into a synthetic gel of SAPO-11 for n-decane hydroisomerization.The mass ratios of ZSM-22/(ZSM-22+SAPO-11)in the composite molecular sieves were optimized and the optimal ZSM-22/SAPO-11 composite(ZS-9)was obtained.The electrostatic repulsions between the ZSM-22 precursors and the SAPO-11 crystalline nuclei produced small ZSM-22 and SAPO-11 crystallites in ZS-9,which increased the specific surface area and mesopore volume and thereby exposed more acid sites.In comparison with conventional SAPO-11,ZSM-22 and their mechanical mixture,ZS-9 with smaller crystallites and the optimal medium and strong Brønsted acid centers(MSBAC)content displayed a higher yield of branched C_(10) isomers(81.6%),lower cracking selectivity(11.9%)and excellent stability.The correlation between the i-C_(10) selectivity and the MSBAC density of molecular sieves indicated that the selectivity for branched C_(10) isomers first increased and then decreased with increasing MSBAC density on the molecular sieves,and the maximum selectivity(87.7%)occurred with a density of 9.6×10^(−2)μmol m^(−2).

A SAPO-11 Silicoaluminophosphate Molecular Sieve with Stable Crystal Structure

A SAPO-11 silicoaluminophosphate molecular sieve with stable crystal structure was synthesized for the first time. After removing template by calcination, its crystal space group still retains Icm2 which the as-synthesized has. The catalyst deriving from the present SAPO-11 materials shows higher isomerization selectivity and higher paraffin hydroisomerization yield than those reported elsewhere.

伊利石合成多级孔SAPO-11分子筛创新实验设计

以伊利石为原料,采用加入介孔模板剂和盐酸酸洗的方法制备了多级孔SAPO-11分子筛,利用XRD、N_(2)吸附-脱附、SEM等方法对样品进行表征。研究结果表明,两种方法均成功制备出多级孔SAPO-11分子筛,与微孔SAPO-11分子筛相比,两种方法得到的多级孔SAPO-11分子筛外表面积和孔体积均明显增大,盐酸酸洗破坏了SAPO-11分子筛的球形晶貌,加入介孔模板剂合成的多级孔SAPO-11分子筛更好地保留了SAPO-11分子筛的晶型结构。具有一定的创新性、综合性和可操作性,有助于提升学生的创新意识和实践能力。

n-Nonane hydroisomerization over hierarchical SAPO-11-based catalysts with sodium dodecylbenzene sulfonate as a dispersant

To enhance the gasoline octane number,low-octane linear n-alkanes should be converted into their high-octane di-branched isomers via n-alkane hydroisomerization.Therefore,hierarchical SAPO-11-based catalysts are prepared by adding different contents of sodium dodecylbenzene sulfonate(SDBS),and they are applied in n-nonane hydroisomerization.When n(SDBS)/n(SiO2)is less than or equal to 0.125,the synthesized hierarchical molecular sieves are all pure SAPO-11,and as the SDBS content increases,the submicron particle size decreases,and the external surface area(ESA)increases.Additionally,these hierarchical SAPO-11 have smaller submicron particles and higher ESA values than conventional SAPO-11.When n(SDBS)/n(SiO2)is greater than 0.125,with increasing SDBS content(n(SDBS)/n(SiO2)=0.25),the synthesized SAPO-11 contains amorphous materials,which leads to a decline in the ESA;with the further increase in SDBS content(n(SDBS)/n(SiO2)=0.5),the products are all amorphous materials.These results indicate that in the case of n(SDBS)/n(SiO2)=0.125,the synthesized SAPO-11 molecular sieve(S–S3)has the most external Brønsted acid centers and the highest ESA of these SAPO-11,and these advantages favor generation of the di-branched isomers in hydrocarbon hydroisomerization.Among these Pt/SAPO-11 catalysts,Pt/S–S3 displays the highest selectivity to entire isomers(83.4%),the highest selectivity to di-branched isomers(28.1%)and the minimum hydrocracking selectivity(15.7%)in n-nonane hydroisomerization.

烃类异构化小粒径、多级孔SAPO-11分子筛催化剂研究进展

由于小粒径、多级孔或兼具小粒径与多级孔结构的SAPO-11分子筛能够显著提高SAPO-11分子筛催化剂在烃类加氢异构化中的活性和选择性,近年来已成为烃类异构化催化剂研究的热点。本文按照SAPO-11分子筛的制备方法进行分类,系统介绍了小粒径、多级孔和兼具小粒径与多级孔结构的SAPO-11分子筛的制备及其临氢异构化性能,指出在今后的研究中,研究开发新的绿色高效合成方法,降低合成成本和减少环境污染是小粒径或(和)多级孔SAPO-11分子筛催化剂实现工业化应用亟待解决的突出问题和研究方向。

Preparation and Property of Ni/TiO₂-SAPO-11 Catalyst for N-Heptane Isomerization

For enhancing the activity of Ni/TiO2-SAPO-11 catalyst, SAPO-11, the precursor was prepared by hydrothermal crystallization, and TiO2-SAPO-11 complex carrier was prepared by sol-gel method, then Ni/TiO2-SAPO-11 was produced by the final product. The catalytic performance of Ni/TiO2-SAPO-11 was studied in n-heptane isomerization, and the impact of catalyst preparation conditions on n-heptane isomerization was discussed in detail. The results showed that, with 20% of TiO2 composition, 2% of Ni capacity percentage and calcined temperature at 500°C, conversion of n-heptane and isomerization selectivity was up to 40.94% and 88.97% respectively.

剑麻纤维素合成多级孔SAPO-11分子筛及其临氢异构化性能

用酸碱处理的剑麻纤维素作为模板剂,采用一步水热法合成多级孔SAPO-11分子筛。对合成分子筛的形貌、孔结构和酸类型进行表征;以正十二烷作为原料,考察Pt负载量为0.5%（质量分数）的SAPO-11分子筛的异构化反应性能。结果表明：利用酸碱处理后的剑麻纤维素合成的多级孔SAPO-11分子筛具有较大的BET比表面积,分子筛中有明显的介孔产生,分子筛孔道内B酸和L酸的比值增加,在正十二烷的临氢异构化反应中表现出更为优异的催化性能。在反应温度为320℃,反应空速为2.0 h^-1,反应压力为2 MPa,氢与油体积比为200：1条件下正十二烷转化率为95.36%时,异构烃收率为69.36%。

Effects of the SAPO-11 synthetic process on dehydration of ethanol to ethylene

The effects of the synthetic condition of SAPO-11 molecular sieves on ethanol dehydration to ethylene were studied.Product-compositions,ethanol conversion,and selectivity to ethylene of synthesized and commercial SAPO-11 molecular sieves were compared.Results are as follows:the optimal synthetic conditions for SAPO-11 molecular sieves are adding pseudoboehmite before orthophoshporic,using di-npropylamine as the template,having a mass fraction of 40%colloidal silica as the silica source and the starting gel obtained,and running at 200℃ for 48 h.From the patterns of NH3-TPD,the amount of acid synthesized by SAPO-11 molecular sieves is less than that by commercial SAPO-11 molecular sieves,and has a stronger weak acid.Also,ethanol conversion and selectivity to ethylene reached 99%at 280℃ on synthesized SAPO-11,lower by 20℃ compared to commercial SAPO-11.For two SAPO-11 molecular sieves,the by-products in the gas phase are mainly ethane,propane,propene,isobutane,n-butane,propadiene,butylene and some higher hydrocarbons.The by-products in the liquid phase are ethyl ether and acetaldehyde.