Production of aromatic hydrocarbons from catalytic fast pyrolysis of microalgae over Fe-modified HZSM-5 catalysts

IF 3.9 3区 化学 Q2 CHEMISTRY, MULTIDISCIPLINARY
RSC Advances Pub Date : 2024-11-20 DOI:10.1039/D4RA06815G
Xinyun Wang, Chuan Li, Jiliang Yang, Yefeng Liu, Jinpei Hei, Shiqi Huang and Daming Gao
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Abstract

In this study, catalytic fast pyrolysis of the microalga C. pyrenoidosa over Fe-modified HZSM-5 catalysts was performed to produce aromatic hydrocarbons using analytical pyrolysis-gas chromatography/mass spectrometry (Py-GC/MS). Fe-modified HZSM-5 catalysts were prepared using wet impregnation and characterized through X-ray diffraction (XRD), scanning electron microscopy (SEM), N2 adsorption–desorption and temperature-programmed desorption of ammonia (NH3-TPD) analysis. The effect of Fe loading (3, 5, 8, and 12 wt%) and pyrolysis temperature (450, 500, 550, 600 °C) on the content of pyrolysis products and the content and selectivity of aromatics was examined. Results showed that the parent HZSM-5 catalyst structure remained intact upon increasing Fe loading, although its specific surface area, micropore volume and average pore diameter decreased. In addition, its external specific surface area and total pore volume increased. The modification of Fe metal increased the total acid amount, especially strong acid sites, which were highest when Fe loading was 8 wt%. The prepared Fe-modified HZSM-5 catalysts exhibited pronounced deoxygenation and denitrogenation effects, which significantly decreased the acid, aldehyde, ketone, furan and nitrogenous compounds, thus improving the production of monocyclic aromatic hydrocarbons (MAHs) while effectively suppressing the formation of polycyclic aromatic hydrocarbons (PAHs). The highest content of aromatic hydrocarbons was obtained with an Fe loading of 8 wt% and pyrolysis temperature of 500 °C, which was 42.5%. As Fe loading increased, benzene selectivity decreased, while the selectivity of toluene and xylene first increased and then decreased. With an increase in pyrolysis temperature, benzene selectivity increased, whereas toluene and xylene selectivity increased at first and then decreased. Reaction mechanisms for the formation of aromatic hydrocarbons during the catalytic pyrolysis of microalgae are put forward. This research revealed that catalytic fast pyrolysis of microalgae over Fe-modified HZSM-5 catalysts is an effective method to produce MAHs.

Abstract Image

在 Fe 改性 HZSM-5 催化剂上催化快速热解微藻类生产芳香烃
本研究采用分析热解-气相色谱/质谱法(Py-GC/MS),在 Fe 改性 HZSM-5 催化剂上对微藻 C. pyrenoidosa 进行催化快速热解,以生产芳香烃。采用湿浸渍法制备了铁改性 HZSM-5 催化剂,并通过 X 射线衍射 (XRD)、扫描电子显微镜 (SEM)、N2 吸附-解吸和氨的温度编程解吸 (NH3-TPD) 分析对其进行了表征。研究了铁含量(3、5、8 和 12 wt%)和热解温度(450、500、550 和 600 °C)对热解产物含量以及芳烃含量和选择性的影响。结果表明,随着铁负载量的增加,母体 HZSM-5 催化剂的结构保持不变,但其比表面积、微孔体积和平均孔径有所减小。此外,其外比表面积和总孔体积有所增加。金属铁的改性增加了总酸量,尤其是强酸位点,当铁的负载量为 8 wt% 时,强酸位点最多。所制备的 Fe 改性 HZSM-5 催化剂具有明显的脱氧和脱氮效果,可显著减少酸、醛、酮、呋喃和含氮化合物,从而提高单环芳烃(MAHs)的产量,同时有效抑制多环芳烃(PAHs)的生成。铁的负载量为 8 wt%、热解温度为 500 °C 时,芳香烃的含量最高,达到 42.5%。随着铁添加量的增加,苯的选择性降低,而甲苯和二甲苯的选择性先增加后降低。随着热解温度的升高,苯的选择性增大,而甲苯和二甲苯的选择性先增大后减小。提出了微藻类催化热解过程中芳香烃形成的反应机理。该研究揭示了在 Fe 改性 HZSM-5 催化剂上催化微藻快速热解是生产 MAHs 的有效方法。
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来源期刊
RSC Advances
RSC Advances chemical sciences-
CiteScore
7.50
自引率
2.60%
发文量
3116
审稿时长
1.6 months
期刊介绍: An international, peer-reviewed journal covering all of the chemical sciences, including multidisciplinary and emerging areas. RSC Advances is a gold open access journal allowing researchers free access to research articles, and offering an affordable open access publishing option for authors around the world.
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