Ni–Pt/H-Y Zeolite Catalysts for Hydroisomerization of n-Hexane and n-Heptane

Ni–Pt/H-Y zeolite catalysts with different Ni contents were prepared and applied to the hydroisomerization of n-hexane and n-heptane in the temperature range 225-375 °C. ESCA studies show the complete reduction of Ni species up to 0.3 wt% Ni addition over 0.1 wt% Pt/H-Y and further addition leads to the occurrence of unreduced nickel species as NiAl₂O₄. A TEM study shows the formation of bimetallic (Ni–Pt) particles of nanoscale size and the average particle size is found to increase with increasing Ni loading. Acidity measurements by NH₃-TPD and pyridine-adsorbed FTIR spectroscopy show the increasing occupation of acid sites by the added nickel when increasing the nickel loading. The catalytic activity of Ni–Pt/H-Y zeolite and Pt/H-Y catalysts was compared and it was found that addition of Ni up to 0.3 wt% increases the n-hexane and n-heptane conversion, multibranched isomer selectivity and sustainability of the catalysts due to better metal-acid synergism, complete reduction of Ni species and the formation of catalytically active Ni–Pt bimetallic particles. Further Ni addition leads to a decrease in conversion and multibranched isomer selectivity and an increase in the cracked products, which may be due to the presence of unreduced Ni species and pore blockage by larger-sized bimetallic particles formed.     

含双金属的超稳Y沸石负载SO2-4/ZrO2强酸性催化剂上正庚烷临氢异构化

用超稳Y沸石（USY）负载SO2-4/ZrO2固体超强酸，并以此为载体制备含Pt双金属催化剂，用XRD和H2-TPR表征了催化剂的物化性质，并在常压固定床反应器上考察催化剂的正庚烷临氢异构化反应性能。结果表明， USY负载了SO2-4/ZrO2和双金属以后仍能保持沸石原有结构；贵金属Pt、金属助剂以及ZrO2等在USY载体上能够高度分散。在含Pt的催化剂中掺杂了Cr或Al金属助剂以后，正庚烷异构化产物选择性有了明显的提高，且具有更好的稳定性和低温活性；在USY负载SO2-4/ZrO2和0.4%Pt的催化剂上，正庚烷的转化率为42.1%时，异构化产物的选择性只有69.6%，而在掺杂了与Pt摩尔比为5∶1的Cr或Al后，正庚烷的转化率分别为44.3%和42.1%时，异构化产物的选择性分别可提高到88.9%和89.5%。     

含层柱皂石加氢异构裂化催化剂的制备及催化性能

通过水热法合成了酸性、孔径适中的层柱皂石材料,并将其经过机械研磨处理后,作为酸性组分通过挤条成型、浸渍Ni-W非贵金属体系,制得了一种新型的加氢异构裂化催化剂。选用正十六烷为模型化合物,以高压釜作为评价装置,与多产低凝柴油的某工业参比催化剂相比,发现在转化率相近时,制备的加氢异构裂化催化剂的加氢异构性能更好。     

A systematic methodology for kinetic modeling of chemical reactions applied to n‐hexane hydroisomerization

Kinetic modeling provides chemical engineers with a unique opportunity to better understand reaction kinetics in general and the underlying chemistry in particular. How to systematically approach a modeling assignment in chemical reaction kinetics is typically less clear, especially for novices in the field. The proposed modeling methodology pursues an adequate compromise between statistical significance and physical meaning of the kinetic model and the corresponding parameters and typically results in models of an appropriate complexity. It comprises the following activities: (1) data analysis, aiming at qualitative information on the reaction mechanism and corresponding rate equations, (2) model regression to quantify this information via optimal parameter values, and (3) validation of the statistical significance and physical meaning of the parameter estimates. This methodology is successfully applied to n‐hexane hydroisomerization on a bifunctional catalyst. © 2014 American Institute of Chemical Engineers AIChE J, 61: 880–892, 2015     

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。     

二甲基萘的异构化方法

本文对二甲基萘的异构化特征和同组内二甲基萘异构化及组与组间二甲基萘加氢异构化方法，进行了全面综述。     

FCC Gasoline Hydroisomerization Over Pt/HZSM-5 Catalysts

Pt/HZSM-5 bifunctional catalyst of fluid catalytic cracking (FCC) gasoline hydroisomerization was prepared. The influence of calcinations and reduction conditions, the metal-incorporation technique, and metal loading on the hydroisomerization of FCC gasoline over the Pt/HZSM-5 bifunctional catalyst was studied. The process opinion catalyst of FCC gasoline hydroisomerization was obtained under the condition of temperature 290-300°C; pressure 1.5-2.5 Mpa; liquid hour space velocity (LHSV) 2.0-3.0 hr^-1; V(H₂)/V(Oil) = 2.0-3.0. The results showed that calcination conditions have a significant influence on ion-exchanged catalysts, as they control the final metal distribution. The reduction conditions and the method used for platinum incorporation were found to be important factors that affected both the activity and selectivity of the catalysts. Pt/HZSM-5 bifunctional catalyst possessed good activity for hydrogenation and isomerization. The olefin hydrocarbons of FCC gasoline were hydrogenated and the stability of FCC gasoline was improved under condition of unchanged octane number.     

Platinum‐promoted fibrous silica Y zeolite with enhanced mass transfer as a highly selective catalyst for n‐dodecane hydroisomerization

A fibrous silica zeolite Y (HY@KCC‐1) catalyst with a high surface area of 568 m²/g and unique core‐shell morphology was successfully synthesized via a modified KCC‐1 synthesis method. Characterization of the catalysts was achieved with X‐ray powder diffraction (XRD), field emission scanning microscope (FESEM), N₂ adsorption/desorption, and 2,6‐dimethylpyridine adsorbed Fourier‐transform infrared spectroscopy (FTIR). The Pt/HY@KCC‐1 has displayed complete n‐dodecane conversion coupled with an incredibly enhanced isomer yield of 72% at 350°C, nearly two‐fold higher than that of unmodified Pt/HY catalyst. Remarkably, Pt/HY@KCC‐1 had an internal effectiveness factor (η) of unity and negligible internal diffusion limitation, thus suggesting its potential application in hydroisomerization of higher hydrocarbons for enhancing fuel properties.