Catalytic combustion of biodiesel wastewater over Fe2O3 catalyst coupled with Pt-based catalyst

IF 3.5 4区 环境科学与生态学 Q3 ENGINEERING, ENVIRONMENTAL Environmental Science: Water Research & Technology Pub Date : 2024-08-01 DOI:10.1039/d4ew00259h
Shangzhi Yu, Wenyu Yuan, Jianfeng Bai, Qinglong Xie, Xiaojiang Liang, Yong Nie
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Abstract

In this paper, biodiesel wastewater was treated by catalytic combustion in the case of catalyst coupling. The effects of reaction temperature, residence time and air flow on the treatment of biodiesel wastewater were investigated using the Fe2O3 catalyst, the Pt/Al2O3@cordierite catalyst and Fe2O3 catalyst coupled with Pt-based catalyst. The effects of high-temperature hydrothermal on two catalysts were evaluated. The catalytic stability was studied in continuous catalytic combustion. Detailed characterization of the two catalysts were carried out. The X-ray fluorescence (XRF), X-ray diffraction (XRD) and X-ray photoelectron spectroscopy (XPS) characterization demonstrated that the Fe2O3 catalyst contained a significant amount of surface active oxygen and Fe2O3 existed in an amorphous form within the catalyst. The Fe2O3 catalyst could remove 90.6% of sulfur in wastewater, showing excellent desulfurization performance, but it was not resistant to high temperature. After 500 °C hydrothermal treatment, the chemical oxygen demand (COD) removal rate decreased significantly from 97.98 % to 69.04 % at the reaction temperature of 280 °C. The COD removal rate of Pt/Al2O3@cordierite catalyst was almost 100% at the reaction temperature of 320 °C, with the activity been basically unchanged after high-temperature hydrothermal treatment, but sulfur poisoning occurred. The Pt/Al2O3@cordierite catalyst coupled with Fe2O3 catalyst showed excellent catalytic activity and stability, and the optimal reaction temperature and residence time were 320 °C and 0.3 s, respectively. In the continuous treatment of biodiesel wastewater with the chemical oxygen demand (COD) of 99465 mg/L for 200 h, the COD and sulfur content of treated wastewater was less than 400 mg/L and 1 mg/L, with the COD removal rate and sulfur removal rate exceeded 99.62% and 81.38%. In addition, no organic gas or SO2 was detected in the exhaust gas generated during the reaction, and the removed organic matter was converted into CO2 and H2O.
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生物柴油废水在 Fe2O3 催化剂和 Pt 催化剂上的催化燃烧
本文在催化剂耦合的情况下,采用催化燃烧法处理生物柴油废水。使用 Fe2O3 催化剂、Pt/Al2O3@堇青石催化剂以及 Fe2O3 催化剂与铂基催化剂耦合,研究了反应温度、停留时间和气流对生物柴油废水处理的影响。评估了高温水热对两种催化剂的影响。在连续催化燃烧中研究了催化稳定性。对两种催化剂进行了详细表征。X 射线荧光 (XRF)、X 射线衍射 (XRD) 和 X 射线光电子能谱 (XPS) 表征表明,Fe2O3 催化剂含有大量表面活性氧,而 Fe2O3 在催化剂中以无定形形式存在。Fe2O3 催化剂可去除废水中 90.6% 的硫,脱硫性能优异,但不耐高温。经过 500 °C 水热处理后,在 280 °C 反应温度下,化学需氧量(COD)去除率从 97.98% 显著下降到 69.04%。在反应温度为 320 ℃ 时,Pt/Al2O3@堇青石催化剂的 COD 去除率接近 100%,高温水热处理后活性基本不变,但出现了硫中毒现象。与 Fe2O3 催化剂偶联的 Pt/Al2O3@cordierite 催化剂表现出优异的催化活性和稳定性,最佳反应温度和停留时间分别为 320 ℃ 和 0.3 s。在连续处理化学需氧量(COD)为 99465 mg/L 的生物柴油废水 200 h 的过程中,处理后废水的 COD 和硫含量分别小于 400 mg/L 和 1 mg/L,COD 去除率和硫去除率分别超过 99.62% 和 81.38%。此外,反应过程中产生的废气中未检测到有机气体或 SO2,去除的有机物被转化为 CO2 和 H2O。
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来源期刊
Environmental Science: Water Research & Technology
Environmental Science: Water Research & Technology ENGINEERING, ENVIRONMENTALENVIRONMENTAL SC-ENVIRONMENTAL SCIENCES
CiteScore
8.60
自引率
4.00%
发文量
206
期刊介绍: Environmental Science: Water Research & Technology seeks to showcase high quality research about fundamental science, innovative technologies, and management practices that promote sustainable water.
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