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合成一种创新的 SF/NZVI 催化剂,并研究其在液化过程中对生物油生产的有效性以及其他参数。

Synthesis of an innovative SF/NZVI catalyst and investigation of its effectiveness on bio-oil production in liquefaction process alongside other parameters.

机构信息

Engineering Faculty, Chemical Engineering Department, Atatürk University, 25240, Erzurum, Turkey.

Engineering Faculty, Chemical Engineering Department, Inonu University, Elazig Road 15Th Km, 44280-Campus, Malatya, Turkey.

出版信息

Environ Sci Pollut Res Int. 2024 Apr;31(19):27913-27934. doi: 10.1007/s11356-024-32981-z. Epub 2024 Mar 25.

Abstract

Today, new energy sources alternative to fossil fuels are needed to meet the increasing energy demand. It is becoming increasingly important to constitute new energy sources from waste biomass through the liquefaction process. In this study, walnut shells (WS) were liquefied catalytically and non-catalytically under different parameters using the liquefaction method. In this process, the effect of silica fume/nano zero-valent iron (SF/NZVI) catalysts on the conversion rates was investigated. The catalyst was synthesized by reducing NZVI using a liquid phase chemical reduction method on SF. The SF/NZVI catalyst was characterized by scanning electron microscopy- energy dispersive X-ray (SEM-EDX), transmission electron microscope (TEM), Brunauer-Emmett-Teller (BET), Fourier transform infrared spectroscopy (FTIR), X-ray diffraction (XRD), and X-ray photoelectron spectroscopy (XPS) analysis. The effect of various process parameters on the liquefaction process was investigated. In this context, the reaction temperature ranged from 300 to 400 °C, the solid/solvent ratio ranged from 1/1 to 1/3, the reaction time ranged from 30 to 90 min, and the catalyst concentration ranged from 1 to 6%. According to the results obtained, the most suitable operating conditions for non-catalytic experiments in liquefaction of WS were found to be temperature of 400 °C, reaction time of 60 min, and solid/solvent of 1/3. In catalytic conditions, the optimum values were obtained as temperature of 375 °C, reaction time of 60 min, solid/solvent ratio of 1/3, and catalyst concentration of 6%. The highest total conversion and (oil + gas) % conversion were 90.4% and 46.7% under non-catalytic conditions and 90.7% and 62.3% under catalytic conditions, respectively. Gas chromatography/mass spectrometry (GC/MS) analysis revealed the bio-oil was mainly composed of aromatic compounds (benzene, butyl-, indane and their derivatives,) and polyaromatic compounds (naphthalene, decahydro-, cis-, naphthalene, 1-methyl-.). The aim of increasing the quantity and quality of the light liquid product in the study has been achieved.

摘要

如今,为了满足不断增长的能源需求,需要寻找替代化石燃料的新能源。通过液化过程,从废生物质中构成新能源变得越来越重要。在这项研究中,核桃壳 (WS) 在不同参数下进行了催化和非催化液化。在这个过程中,研究了硅灰/纳米零价铁 (SF/NZVI) 催化剂对转化率的影响。该催化剂是通过在 SF 上使用液相化学还原法还原 NZVI 合成的。SF/NZVI 催化剂通过扫描电子显微镜-能量色散 X 射线 (SEM-EDX)、透射电子显微镜 (TEM)、BET、傅里叶变换红外光谱 (FTIR)、X 射线衍射 (XRD) 和 X 射线光电子能谱 (XPS) 分析进行了表征。研究了各种工艺参数对液化过程的影响。在这方面,反应温度范围为 300 至 400°C,固/溶剂比范围为 1/1 至 1/3,反应时间范围为 30 至 90 分钟,催化剂浓度范围为 1 至 6%。根据获得的结果,发现 WS 液化中非催化实验的最适宜操作条件为温度 400°C、反应时间 60 分钟、固/溶剂比 1/3。在催化条件下,最佳值为温度 375°C、反应时间 60 分钟、固/溶剂比 1/3、催化剂浓度 6%。在非催化条件下,总转化率和(油+气)转化率最高分别为 90.4%和 46.7%,在催化条件下最高分别为 90.7%和 62.3%。气相色谱/质谱 (GC/MS) 分析表明,生物油主要由芳香族化合物(苯、丁基、茚满和它们的衍生物)和多环芳烃(萘、十氢、顺式、萘、1-甲基-。)组成。研究的目的是提高轻质液体产物的数量和质量。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/6229/11058616/4215c69862e3/11356_2024_32981_Fig1_HTML.jpg

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