DOI: 10.57760/sciencedb.j00124.00441
title: The Data of Influence of the Acidity on the Performance of Propylene Oligomerization over HZSM-5 Catalysts
title: The Data of Influence of the Acidity on the Performance of Propylene Oligomerization over HZSM-5 Catalysts

description: The dataset mainly includes a graphical abstract and characterization data of the physicochemical structure of HZSM-5 zeolites with different silica-to-alumina ratios, as well as evaluation data of their catalytic performance in propylene oligomerization.(1) Graphical Abstract: This figure primarily summarizes the content abstract of the submission to the Journal of Fuel Chemistry and Technology (Chinese and English editions).(2) Physicochemical Characterization Data of Self-Synthesized HZSM-5 Zeolite Catalysts:Figure 1: XRD characterization data of the zeolite crystal structure, obtained using a Bruker D8 ADVANCE X-ray diffractometer. This data primarily investigates the crystal structure of HZSM-5 zeolites.Figure 2: SEM characterization of the catalyst samples, performed using a Carl Zeiss Gemini360 field emission scanning electron microscope. It shows the morphology of the HZSM-5 zeolite catalysts, labeled as SEM (a), SEM (b), SEM (c), and SEM (d). These images visually display the hexagonal prism morphology and grain dispersion degree of four zeolites with different silica-to-alumina ratios: HZSM-5-30, HZSM-5-50, HZSM-5-90, and HZSM-5-120.Figure 3: Nitrogen physisorption measurements conducted using a Microtrac MRB Belsorp max X analyzer. This figure presents the adsorption-desorption isotherms of HZSM-5-30, HZSM-5-50, HZSM-5-90, and HZSM-5-120 zeolites with different silica-to-alumina ratios. It shows the actual gas adsorption capacity of the samples under different pressures and represents the raw experimental data for BET analysis.Figure 4: NH3-TPD desorption curves. Acidity characterization was performed using NH₃ temperature-programmed desorption. This figure mainly shows the NH₃ desorption curves of HZSM-5-30, HZSM-5-50, HZSM-5-90, and HZSM-5-120 zeolites with increasing temperature, characterizing the acid amount and acid strength of the catalysts.Figure 5: Py-FTIR spectra of HZSM-5 catalysts with different silica-to-alumina ratios, used to analyze the types of acid sites in HZSM-5-30, HZSM-5-50, HZSM-5-90, and HZSM-5-120 zeolites.Figure 6: Evaluation of propylene oligomerization performance for HZSM-5 catalysts with different silica-to-alumina ratios at various reaction temperatures. The data were obtained from temperature-programmed evaluation in a fixed-bed reactor. The x-axis represents temperature, and the y-axis represents the oil yield from propylene oligomerization.Figure 7: Product distribution of HZSM-5 catalysts with different silica-to-alumina ratios at the maximum oil yield, mainly including carbon number distribution and product type distribution. The data were obtained from a fixed-bed evaluation unit. This primarily investigates the effect of the silica-to-alumina ratio (acidity) on the product distribution and carbon number distribution of propylene oligomerization over HZSM-5 zeolites.
description: The dataset mainly includes a graphical abstract and characterization data of the physicochemical structure of HZSM-5 zeolites with different silica-to-alumina ratios, as well as evaluation data of their catalytic performance in propylene oligomerization.(1) Graphical Abstract: This figure primarily summarizes the content abstract of the submission to the Journal of Fuel Chemistry and Technology (Chinese and English editions).(2) Physicochemical Characterization Data of Self-Synthesized HZSM-5 Zeolite Catalysts:Figure 1: XRD characterization data of the zeolite crystal structure, obtained using a Bruker D8 ADVANCE X-ray diffractometer. This data primarily investigates the crystal structure of HZSM-5 zeolites.Figure 2: SEM characterization of the catalyst samples, performed using a Carl Zeiss Gemini360 field emission scanning electron microscope. It shows the morphology of the HZSM-5 zeolite catalysts, labeled as SEM (a), SEM (b), SEM (c), and SEM (d). These images visually display the hexagonal prism morphology and grain dispersion degree of four zeolites with different silica-to-alumina ratios: HZSM-5-30, HZSM-5-50, HZSM-5-90, and HZSM-5-120.Figure 3: Nitrogen physisorption measurements conducted using a Microtrac MRB Belsorp max X analyzer. This figure presents the adsorption-desorption isotherms of HZSM-5-30, HZSM-5-50, HZSM-5-90, and HZSM-5-120 zeolites with different silica-to-alumina ratios. It shows the actual gas adsorption capacity of the samples under different pressures and represents the raw experimental data for BET analysis.Figure 4: NH3-TPD desorption curves. Acidity characterization was performed using NH₃ temperature-programmed desorption. This figure mainly shows the NH₃ desorption curves of HZSM-5-30, HZSM-5-50, HZSM-5-90, and HZSM-5-120 zeolites with increasing temperature, characterizing the acid amount and acid strength of the catalysts.Figure 5: Py-FTIR spectra of HZSM-5 catalysts with different silica-to-alumina ratios, used to analyze the types of acid sites in HZSM-5-30, HZSM-5-50, HZSM-5-90, and HZSM-5-120 zeolites.Figure 6: Evaluation of propylene oligomerization performance for HZSM-5 catalysts with different silica-to-alumina ratios at various reaction temperatures. The data were obtained from temperature-programmed evaluation in a fixed-bed reactor. The x-axis represents temperature, and the y-axis represents the oil yield from propylene oligomerization.Figure 7: Product distribution of HZSM-5 catalysts with different silica-to-alumina ratios at the maximum oil yield, mainly including carbon number distribution and product type distribution. The data were obtained from a fixed-bed evaluation unit. This primarily investigates the effect of the silica-to-alumina ratio (acidity) on the product distribution and carbon number distribution of propylene oligomerization over HZSM-5 zeolites.