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学者姓名：王廷海
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Abstract ：
In order to gain insight into the influence of SiO2 support particle size on the vacuum residue (VR) slurry-phase hydrocracking performance of Fe-based catalysts, a series of FeZn/SiO2 catalysts with varying SiO2 particle sizes were prepared. Characterization results show that the surface area and pore volume of the FeZn/SiO2 catalysts increase with the reduction of SiO2 particle sizes. The metals Fe and Zn species on FeZn/SiO2-S catalyst are more readily reducible via H2-TPR analysis. Notably, FeZn/SiO2-S catalyst presents higher metal dispersion and a greater degree of sulfurization compared to the other catalysts by XRD and XPS. Hydrocracking results demonstrate that the FeZn/SiO2-S catalyst achieves the lowest coke and gas yields (11.9 wt% and 0.4 wt%), respectively, and the highest VR conversion among these catalysts. The superior performance of the FeZn/SiO2-S catalyst in VR slurry-phase hydrocracking is ascribed to its enhanced hydrogenation activity, deriving from the higher dispersion and sulfurization of metals species. This suppresses the aggregation of polycyclic aromatic hydrocarbons in VR and the over-cracking of intermediate products. Additionally, the increased mesopore associated with smaller SiO2 particles facilitates to the diffusion of large VR molecules, further promoting the hydrocracking reaction.
Keyword ：
FeZn catalyst FeZn catalyst Hydrogenation activity Hydrogenation activity SiO2 particle size SiO2 particle size Slurry-phase hydrocracking Slurry-phase hydrocracking Vacuum residue Vacuum residue
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| GB/T 7714 | Wang, Jianbo , Yan, Jianteng , Cui, Qingyan et al. Effect of SiO2 support particle sizes on the performance of FeZn catalysts in VR slurry-phase hydrocracking [J]. | CATALYSIS TODAY , 2025 , 449 . |
| MLA | Wang, Jianbo et al. "Effect of SiO2 support particle sizes on the performance of FeZn catalysts in VR slurry-phase hydrocracking" . | CATALYSIS TODAY 449 (2025) . |
| APA | Wang, Jianbo , Yan, Jianteng , Cui, Qingyan , Li, Tiesen , Shi, Jie , Wang, Tinghai et al. Effect of SiO2 support particle sizes on the performance of FeZn catalysts in VR slurry-phase hydrocracking . | CATALYSIS TODAY , 2025 , 449 . |
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The catalytic cracking gasoline with high sulfur and high olefin content accounts for about 60% of the gasoline pool in China. Therefore, ultra-deep selective hydrodesulfurization of catalytic cracking gasoline and the protection of olefins from hydrogenation saturation are still the key technical problems to be solved in the production of high octane gasoline for a long time in the future. During the decades of the development of fluid catalytic cracking gasoline hydrodesulfurization, researchers have systematically investigated the distribution of sulfur species and hydrocarbon composition, process technology, active phase structure, promoter effect and mass transfer. From the view of mass transfer, this paper innovatively adopted the method of adjusting aging time, prepared a series of eggshell type catalysts in a controllable way. The performance of these catalysts for ultra-deep selective hydrodesulfurization of fluid catalytic cracking gasoline was investigated. A new concept was provided for the design and development of fluid catalytic cracking gasoline hydrodesulfurization catalysts. The catalysts were characterized by SEM-EDX, XRD, H2-TPR, N2 adsorption-desorption, XPS and HRTEM. The SEM-EDX results showed that the Mo element was an eggshell type distribution in the catalyst while the Co element evenly distributed in the catalyst. The thickness of eggshell increased gradually with the extension of aging time and Mo elements tended to be evenly distributed until the aging time is 95 min. The reason was that the Co element existed as Co2+ while the Mo and P element formed [Mo12O40P]3− complex in the solution. The migration rate of [Mo12O40P]3− complex in the catalyst pores was slow during impregnation while the Co2+ migrating fast. The SEM-EDX results indicated that the eggshell thickness of catalyst could be adjusted by controlling aging time. The XRD and H2-TPR results showed that the eggshell distribution of Mo did not change the dispersibility of the active metals. The N2 adsorption/desorption results showed that the aging time had little effect on the pore structure of the catalysts. The XPS results showed that the content of Mo4+ and Co-Mo-S on catalyst surface decreased with the increasing of eggshell thickness, it may be due to the migration of Mo element into the interior of the catalyst, resulting in a decrease in the concentration of Mo element on the surface of the catalyst. The HRTEM results showed that the eggshell thickness had a slight effect on the length and number of layers of MoS2, but with the increase of eggshell thickness, the proportion of fe/fc in the catalyst decreases slightly. Finally, model catalytic cracking gasoline was used to investigate the desulfurization performance of the catalyst. The results showed that the eggshell type catalyst had little effect on desulfurization activity, but the eggshell type catalyst had lower olefin saturation activity. At different reaction temperatures, with the increase of the eggshell thickness, the desulfurization selectivity of the catalyst gradually decreased which mainly due to the fact that the eggshell catalyst had a higher fe/fc, while the lower mass transfer resistance made the olefin molecules stay in the shell containing the Mo active phase for a shorter time. © 2025 Science Press. All rights reserved.
Keyword ：
Diffusion in gases Diffusion in gases Diffusion in liquids Diffusion in liquids Diffusion in solids Diffusion in solids Fluid catalytic cracking Fluid catalytic cracking Hydrocracking Hydrocracking Hydrodesulfurization Hydrodesulfurization Hydrogenation Hydrogenation Osmosis Osmosis Thermal diffusion Thermal diffusion
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| GB/T 7714 | Xu, Jingdong , Li, Wentao , Li, Huisheng et al. Controllable preparation and hydrodesulfurization performance of eggshell type Co/Mo catalyst [J]. | Journal of Fuel Chemistry and Technology , 2025 , 53 (5) : 725-732 . |
| MLA | Xu, Jingdong et al. "Controllable preparation and hydrodesulfurization performance of eggshell type Co/Mo catalyst" . | Journal of Fuel Chemistry and Technology 53 . 5 (2025) : 725-732 . |
| APA | Xu, Jingdong , Li, Wentao , Li, Huisheng , Ai, Zilong , Wang, Tinghai , Xu, Renwei . Controllable preparation and hydrodesulfurization performance of eggshell type Co/Mo catalyst . | Journal of Fuel Chemistry and Technology , 2025 , 53 (5) , 725-732 . |
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催化裂化汽油超深度加氢脱硫和保护烯烃不被加氢饱和为烷烃,依然是中国汽油质量升级的技术需求.本论文从传质角度出发,设计并制备了蛋壳型加氢脱硫催化剂,采用调控陈化时间的方法,可控制备了一系列的蛋壳型催化剂.采用 SEM-EDX、XRD、H2-TPR、N2 吸附-脱附、XPS和 HRTEM对 催化剂进行表征.表征结果表明,制备的蛋壳型催化剂具有蛋壳厚度可调、蛋壳分布均匀的优点;蛋壳厚度对层状结构MoS2 的片层长度和层数略有影响,但随着蛋壳厚度的增加,催化剂中Edge边位比例(fe)和Rim角位比例(fc)的比值fe/fc略有降低.选用模型催化裂化汽油对催化剂的脱硫性能进行考察,蛋壳型催化剂对脱硫活性影响较小,但蛋壳型催化剂具有更低的烯烃饱和活性,这主要归因于蛋壳催化剂具有更高的fe/fc,同时更低的传质阻力使得烯烃分子在含Mo活性相的壳层停留时间缩短.
Keyword ：
催化裂化汽油 催化裂化汽油 加氢脱硫 加氢脱硫 蛋壳催化剂 蛋壳催化剂 选择性 选择性
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| GB/T 7714 | 徐景东 , 李文涛 , 李慧胜 et al. 蛋壳型Co/Mo催化剂的可控制备及其加氢脱硫性能 [J]. | 燃料化学学报（中英文） , 2025 , 53 (5) : 725-732 . |
| MLA | 徐景东 et al. "蛋壳型Co/Mo催化剂的可控制备及其加氢脱硫性能" . | 燃料化学学报（中英文） 53 . 5 (2025) : 725-732 . |
| APA | 徐景东 , 李文涛 , 李慧胜 , 艾子龙 , 王廷海 , 徐人威 . 蛋壳型Co/Mo催化剂的可控制备及其加氢脱硫性能 . | 燃料化学学报（中英文） , 2025 , 53 (5) , 725-732 . |
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A seed-directed approach to synthesizing FeZSM-22 zeolite without organic structure directing agent(OSDA)was developed by using Fe-rich diatomite as all aluminum and iron sources.The FeZSM-22 zeolite with optimal crystallinity and purity can be obtained by systematically adjusting feed composi-tion and synthesis conditions.Characterizations show that FeZSM-22 zeolite synthesized with OSDA-free owns high crystallinity,obvious thin needle-shaped morphology and high Bronsted/Lewis acid ratio.Significantly,when used for n-octane hydroisomerization reaction,its derived catalyst exhibits the best catalytic performance reflected by the highest selectivity to C8 isomers compared to the two reference catalysts prepared based on a Fe-containing and a Fe-free ZSM-22 synthesized through an OSDA-directed route from natural diatomite and conventional chemicals,respectively.This work provides an alternative route to sustainably synthesizing heteroatomic zeolites with high performance.
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| GB/T 7714 | Tiesen Li , Ting Chen , Yinghui Ye et al. OSDA-free synthesis of FeZSM-22 zeolite from natural minerals for n-octane hydroisomerization [J]. | 中国化学工程学报（英文版） , 2024 , 66 (2) : 51-59 . |
| MLA | Tiesen Li et al. "OSDA-free synthesis of FeZSM-22 zeolite from natural minerals for n-octane hydroisomerization" . | 中国化学工程学报（英文版） 66 . 2 (2024) : 51-59 . |
| APA | Tiesen Li , Ting Chen , Yinghui Ye , Peng Dong , Tinghai Wang , Qingyan Cui et al. OSDA-free synthesis of FeZSM-22 zeolite from natural minerals for n-octane hydroisomerization . | 中国化学工程学报（英文版） , 2024 , 66 (2) , 51-59 . |
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FAU型分子筛因其独特的孔道结构已成为化学工业中应用最广泛、用量最大的催化剂、催化剂载体及吸附剂之一.然而, FAU型分子筛单一的微孔孔道限制了客体分子的扩散,导致其性能严重下降.相比之下,等级孔FAU型分子筛具有微-介/大孔复合的多级孔道结构,能够促进大分子的扩散、提高活性位点的可接近性,进而改善其吸附和催化性能.目前,等级孔分子筛的制备方法主要包括“自下而上”的直接合成法和“自上而下”的后处理法.本文主要介绍了近年来等级孔X型和Y型分子筛制备方法的研究现状,重点总结了等级孔X型和Y型分子筛在吸附、催化等过程中的应用性能,并对等级孔FAU型分子筛的绿色化制备进行展望.
Keyword ：
催化 催化 后处理 后处理 吸附 吸附 直接合成 直接合成 等级孔FAU型分子筛 等级孔FAU型分子筛
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| GB/T 7714 | 董鹏 , 朱琳 , 骆龙华 et al. 等级孔FAU型分子筛的制备及应用的研究进展 [J]. | 科学通报 , 2024 , 69 (19) : 2718-2728 . |
| MLA | 董鹏 et al. "等级孔FAU型分子筛的制备及应用的研究进展" . | 科学通报 69 . 19 (2024) : 2718-2728 . |
| APA | 董鹏 , 朱琳 , 骆龙华 , 李铁森 , 王廷海 , 王婵 et al. 等级孔FAU型分子筛的制备及应用的研究进展 . | 科学通报 , 2024 , 69 (19) , 2718-2728 . |
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Abstract ：
A seed-directed approach to synthesizing FeZSM-22 zeolite without organic structure directing agent (OSDA) was developed by using Fe-rich diatomite as all aluminum and iron sources. The FeZSM-22 zeolite with optimal crystallinity and purity can be obtained by systematically adjusting feed composition and synthesis conditions. Characterizations show that FeZSM-22 zeolite synthesized with OSDA-free owns high crystallinity, obvious thin needle-shaped morphology and high Bronsted/Lewis acid ratio. Significantly, when used for n-octane hydroisomerization reaction, its derived catalyst exhibits the best catalytic performance reflected by the highest selectivity to C-8 isomers compared to the two reference catalysts prepared based on a Fe-containing and a Fe-free ZSM-22 synthesized through an OSDA-directed route from natural diatomite and conventional chemicals, respectively. This work provides an alternative route to sustainably synthesizing heteroatomic zeolites with high performance. (c) 2023 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd. All rights reserved.
Keyword ：
FeZSM-22 zeolite FeZSM-22 zeolite Natural minerals Natural minerals n-octane hydroisomerization n-octane hydroisomerization OSDA-free synthesis OSDA-free synthesis
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| GB/T 7714 | Li, Tiesen , Chen, Ting , Ye, Yinghui et al. OSDA-free synthesis of FeZSM-22 zeolite from natural minerals for n-octane hydroisomerization [J]. | CHINESE JOURNAL OF CHEMICAL ENGINEERING , 2024 , 66 : 51-59 . |
| MLA | Li, Tiesen et al. "OSDA-free synthesis of FeZSM-22 zeolite from natural minerals for n-octane hydroisomerization" . | CHINESE JOURNAL OF CHEMICAL ENGINEERING 66 (2024) : 51-59 . |
| APA | Li, Tiesen , Chen, Ting , Ye, Yinghui , Dong, Peng , Wang, Tinghai , Cui, Qingyan et al. OSDA-free synthesis of FeZSM-22 zeolite from natural minerals for n-octane hydroisomerization . | CHINESE JOURNAL OF CHEMICAL ENGINEERING , 2024 , 66 , 51-59 . |
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FAU-type zeolites are an important class of porous aluminosilicate materials with a 3-dimiensional network of accessible micropores (0.74 nm), which primarily encompass X and Y zeolites. Typically, FAU zeolite with a framework SiO2/Al(2)O3 molar ratio between 2.0 and 3.0 is called X zeolite, and that is greater than 3.0 is classified as Y zeolite. Due to their distinctive structure and pore characteristics, FAU-type zeolites have emerged as one of the most widely used catalysts, catalyst carriers, and adsorbents in the chemical industry. However, the sole microporous channels of the conventional FAU-type zeolites not only make them difficult for the reactions involving bulky molecules to occur within pore channel, leading to insufficient contact between reactants with active sites of the zeolite, but also restrict the diffusion of product within the zeolite, thus affecting the activity and lifetime of the catalyst. Therefore, the key to improving the performance of FAU-type zeolites lies in alleviating the adverse effects of micropore diffusion on mass transfer. Introducing mesopores and/or macropores into microporous zeolites to construct hierarchical zeolites with a multi-modal pore structure is believed to be a promising approach. This modification not only can preserve the active sites from the microporous structure, but also significantly enhances the diffusion rate of guest molecules within the zeolites. Consequently, researchers have concentrated on the preparation and application of hierarchical zeolites. This article focuses on the current research status on the preparation of hierarchical X and Y zeolites based on "bottom-up" direct synthesis and "top-down" post-treatment methods. The direct synthesis method mainly comprises template and template-free methods. In terms of the template method, the pore structure of FAU zeolites can be tailored by altering the nature of the templating agent, synthesis conditions and so on. Differently, the template-free method enables the preparation of hierarchical FAU zeolites without the addition of any template. In particular, hierarchical X and Y zeolites have been successfully synthesized directly from natural aluminosilicate minerals without the use of organic templates, which not only reduces the synthesis cost of hierarchical zeolites from raw materials, but also contributes to environmental protection. This method provides a novel synthetic pathway for the preparation of hierarchical zeolites in a low-cost and green way. On the other hand, posttreatment method based on desilication and dealumination is the main method for the preparation of hierarchical Y zeolite, whereas few researchers have made use of post-treatment method to introduce meso/macroporous structures into X zeolite because of the poor chemical stability of X zeolite. In addition, the article introduces the application performance of hierarchical X and Y zeolites in adsorption, catalysis as well as other reaction processes. Despite the superior diffusion capabilities of hierarchical FAU-type zeolites, there are several problemsincluding high cost of organic templates and pollution emissions from the removal of template in the process of synthesizing hierarchical zeolites based on template method, limiting the industrial application of this method. As a result, designing cheap and recyclable templates is the key to realizing green and low-cost preparation of hierarchical FAU-type zeolite. Furthermore, post-treatment method cannot achieve the regulation of mesoporous size in hierarchical zeolites. Future research should deeply investigate the structureactivity relationship between the pore structure and reaction performance of hierarchical FAU-type zeolites, so as to further open pore channels, and enhance diffusion, thus promoting the development of hierarchical FAU-type zeolites in industrial applications.
Keyword ：
adsorption adsorption catalysis catalysis direct synthesis direct synthesis hierarchical FAU-type zeolites hierarchical FAU-type zeolites post treatment post treatment
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| GB/T 7714 | Dong, Peng , Zhu, Lin , Luo, Longhua et al. Research progress in the synthesis and application of hierarchical FAU-type zeolites [J]. | CHINESE SCIENCE BULLETIN-CHINESE , 2024 , 69 (19) : 2718-2728 . |
| MLA | Dong, Peng et al. "Research progress in the synthesis and application of hierarchical FAU-type zeolites" . | CHINESE SCIENCE BULLETIN-CHINESE 69 . 19 (2024) : 2718-2728 . |
| APA | Dong, Peng , Zhu, Lin , Luo, Longhua , Li, Tiesen , Wang, Tinghai , Wang, Chan et al. Research progress in the synthesis and application of hierarchical FAU-type zeolites . | CHINESE SCIENCE BULLETIN-CHINESE , 2024 , 69 (19) , 2718-2728 . |
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To gain a profound understanding of the reaction pathway and the controlling step of residue oil slurry-phase hydrocracking over Fe2O3 catalyst, a six-lumped kinetic model was proposed and employed to acquire the kinetic rate constants based on each fraction yield obtained at 400 to 420 degrees C under initial H2 pressures of 8 to 10 MPa for 1 to 3 h. The optimal kinetic rate constant for each step of vacuum residue (VR) conversion process was determined via Levenberg-Marquardt algorithm and the sum of squares error (SSE). The results reveal that VR converted into naphtha and diesel is dominant according to their kinetic rate constants, followed by the conversion of vacuum gas oil (VGO) to diesel, diesel to naphtha, and diesel to gas. Furthermore, the sensitivity analysis confirms a strong agreement between the predicted and experimental values. The combination of kinetic rate constants and activation energy illustrates that the gas product primarily originates from naphtha. Additionally, the higher H2 pressure effectively mitigates coke deposition by restricting the aggregation of polycyclic aromatics, as evidenced by the increase in the reaction activation energy for the conversion of VR to coke and the analysis of the used catalyst.
Keyword ：
Kinetics Kinetics Lumped models Lumped models Slurry-phase hydrocracking Slurry-phase hydrocracking
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| GB/T 7714 | Cui, Qingyan , Zheng, Bin , Wang, Boshi et al. Kinetics study on residue oil slurry-phase hydrocracking with Fe2O3 catalyst [J]. | FUEL , 2024 , 374 . |
| MLA | Cui, Qingyan et al. "Kinetics study on residue oil slurry-phase hydrocracking with Fe2O3 catalyst" . | FUEL 374 (2024) . |
| APA | Cui, Qingyan , Zheng, Bin , Wang, Boshi , Yan, Jianteng , Liu, Jiangyong , Li, Tiesen et al. Kinetics study on residue oil slurry-phase hydrocracking with Fe2O3 catalyst . | FUEL , 2024 , 374 . |
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Cyclohexane as liquid organic hydrogen carriers has attracted considerable interest in the field of hydrogen storage technology. However, the innovation of efficient catalyst for producing H2 through cyclohexane dehydrogenation remains a substantial challenge. In this study, we have successfully developed Pt/MgAl2O4 catalysts exhibiting outstanding catalytic performance in cyclohexane dehydrogenation. Notably, the optimal catalyst Pt/ MgAl2O4-700 achieves cyclohexane conversion of 89.1 % and benzene selectivity of over 99 % at 345 degrees C, resulting in a high hydrogen evolution rate of 933 mmol/gPt/min. Moreover, this catalyst exhibits remarkable long-term stability, with no evident loss of activity in 225-hour dehydrogenation reaction. The catalyst was characterized by XRD, N2 adsorption-desorption, STEM, XPS, NH3-TPD, CO-FTIR and H2-TPR techniques, which provides detailed structure information for elucidation of structure-activity relationship. The spinel structure and moderate acid density of the support enable highly dispersed Pt species at the surface of MgAl2O4. This results in the formation of ultra-small and sintering-resistant Pt particles that exhibit exceptional activity in cyclohexane dehydrogenation. Additionally, the presence of positively charged Pt delta+ species in Pt/MgAl2O4 facilitates the rapid desorption of benzene product. This effectively prevents the formation of coke arising from benzene dehydrogenation, which ensures to achieve high stability. These findings provide valuable knowledge for the rational design of efficient metal-based catalysts for liquid organic hydrogen carriers in hydrogen storage systems.
Keyword ：
Cyclohexane dehydrogenation Cyclohexane dehydrogenation H-2 production H-2 production Liquid organic hydrogen carriers Liquid organic hydrogen carriers Positively charged Pt Positively charged Pt Pt/MgAl2O4 Pt/MgAl2O4
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| GB/T 7714 | Guo, Lipeng , Xu, Zhikang , Wang, Tinghai et al. Stable Pt/MgAl2O4 catalysts for efficient production of H2 from cyclohexane dehydrogenation [J]. | CHEMICAL ENGINEERING SCIENCE , 2024 , 299 . |
| MLA | Guo, Lipeng et al. "Stable Pt/MgAl2O4 catalysts for efficient production of H2 from cyclohexane dehydrogenation" . | CHEMICAL ENGINEERING SCIENCE 299 (2024) . |
| APA | Guo, Lipeng , Xu, Zhikang , Wang, Tinghai , Zhu, Haibo . Stable Pt/MgAl2O4 catalysts for efficient production of H2 from cyclohexane dehydrogenation . | CHEMICAL ENGINEERING SCIENCE , 2024 , 299 . |
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The catalytic dehydration of glycerol to acrolein offers a sustainable route for efficiently utilizing low-cost and renewable bioglycerol. This work deeply explores glycerol dehydration to acrolein over ZSM-5 zeolite catalysts with various pore structures and aluminum distributions. The results reveal that glycerol conversion is enhanced through the construction of a mesoporous structure and the increase in Br & oslash;nsted acid sites of the catalysts, but acrolein selectivity is not directly related to these factors. Further characterizations, density functional theory calculation, kinetic study, and reaction mechanism analysis demonstrate that the richest Alsingle sites in the zeolite framework and the least Alpair sites in the straight and sinusoidal channels can prevent the generated acrolein from adsorbing on adjacent Al sites. This allows acrolein to immediately escape from the catalyst surface, reducing side reactions and enhancing its selectivity. Therefore, the synergistic between the mesoporous structure and more Alsingle sites in the ZSM-5 zeolite framework promotes acrolein yield. Additionally, a descriptor phi, reflecting the amount of Alsingle sites and the external specific surface area of the ZSM-5 zeolite, is first proposed to more clearly elucidate the structure-performance relationship. This study provides a new perspective for understanding the mechanism of catalytic dehydration of glycerol to acrolein, guiding the development of highly efficient catalysts. It is significant for the sustainable development of the biodiesel and acrolein production industry.
Keyword ：
aluminum distribution aluminum distribution catalytic dehydration catalytic dehydration glycerol glycerol pore structure pore structure ZSM-5 zeolitecatalyst ZSM-5 zeolitecatalyst
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| GB/T 7714 | Luo, Wei , Shi, Jie , Li, Tiesen et al. Catalytic Dehydration of Glycerol to Acrolein over ZSM-5 Zeolites: Synergistic Effect of Pore Structure and Aluminum Distribution [J]. | ACS SUSTAINABLE CHEMISTRY & ENGINEERING , 2024 , 13 (1) : 321-332 . |
| MLA | Luo, Wei et al. "Catalytic Dehydration of Glycerol to Acrolein over ZSM-5 Zeolites: Synergistic Effect of Pore Structure and Aluminum Distribution" . | ACS SUSTAINABLE CHEMISTRY & ENGINEERING 13 . 1 (2024) : 321-332 . |
| APA | Luo, Wei , Shi, Jie , Li, Tiesen , Wang, Tinghai , Liu, Jiangyong , Cui, Qingyan et al. Catalytic Dehydration of Glycerol to Acrolein over ZSM-5 Zeolites: Synergistic Effect of Pore Structure and Aluminum Distribution . | ACS SUSTAINABLE CHEMISTRY & ENGINEERING , 2024 , 13 (1) , 321-332 . |
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