Effect of Organic Acids on Ultrasonication-assisted Removal of Harmful Metals from Spent FCC Catalysts
YU Yusen1,2, LE Thiquynhxuan1,2,*, WANG Tian1,2, ZHANG Libo1,2
1 State Key Laboratory of Complex Nonferrous Metal Resources Clean Utilization, Kunming University of Science and Technology, Kunming 650093, China 2 Faculty of Metallurgical and Energy Engineering, Kunming University of Science and Technology, Kunming 650093, China
Abstract: The main causes of poisoning of fluid catalytic cracking (FCC) catalysts in the petroleum industry are harmful metals, such as Fe, V and Ni, which reduce the activity of the FCC catalysts. The existing regeneration processes of spent FCC catalysts have problems, such as low metal removal rate, incomplete microstructure, and damaged zeolite Y framework, resulting in the inability of spent FCC catalysts to be reused. An effective method combining organic acids as a leaching agent and ultrasonic radiation was developed in this study to improve the removal effect of harmful metals in spent FCC catalyst without destroying the zeolite Y framework and particle microstructure. The effects of oxidation pretreatment, organic acid type, leaching temperature, leaching time, and ultrasonic power on the zeolite Y framework, particle microstructure, and harmful metal removal were investigated. The experimental results show that the removal effects of different organic acids on harmful metals under ultrasound are in the order from weak to strong as follows: acetic acid, EDTA, oxalic acid + acetic acid, oxalic acid, and the destruction of the microstructure of the spent catalyst particle increases in this order. After leaching in a mixture of oxalic acid and acetic acid for 30 min at 70 ℃ with an ultrasonic power of 250 W, a regenerated catalyst with a complete particle structure and zeolite Y framework was obtained, with the removal rates of V, Fe and Ni 40.7%, 27.5% and 17.2%, respectively. Compared to conventional leaching, ultrasonic leaching exhibited a strengthening effect on removing harmful metals, and the leaching rates of V, Fe and Ni increased by 19.9%, 13.1% and 7.7%, respectively, during the ultrasonic leaching process.
1 Wang J Y, Huang X W, Wang L S, et al. Hydrometallurgy, 2017, 171, 312. 2 Vogt E T C , Weckhuysen B M. Chemical Society Reviews, 2015, 44, 7342. 3 Bin D H, Zhu X M, Fu H H, et al. Journal of Environmental Enginee-ring Technology, 2019, 9(4), 453 (in Chinese). 宾灯辉, 朱雪梅, 傅海辉, 等. 环境工程技术学报, 2019, 9(4), 453. 4 National Hazardous Waste List (2021 edition). Communiqué of the State Council of the People's Republic of China, 2021(4), 18 (in Chinese). 国家危险废物名录(2021年版). 中华人民共和国国务院公报, 2021(4), 18. 5 Zhao Z X, Qiu Z F, Yang J, et al. Hydrometallurgy, 2017, 167, 183. 6 Huang Y Y, Wang L L, Chen X P, et al. Guangxi Sciences, 2015, 22(1), 65 (in Chinese). 黄莹莹, 王琳琳, 陈小鹏, 等. 广西科学, 2015, 22(1), 65. 7 Ferella F, Innocenzi V, Maggiore F. Resources Conservation & Recycling, 2016, 108, 10. 8 Velázquez S, Monzó J, Borrachero M V, et al. Thermochimica Acta, 2016, 632, 29. 9 Qi L. Adsorption of bisphnol compounds in aqueous solution by spent FCC catalyst. Master's Thesis, Liaoning Shihua University, China, 2019 (in Chinese). 戚霖. 废FCC催化剂吸附水溶液中的双酚类化合物. 硕士学位论文, 辽宁石油化工大学, 2019. 10 Zhang J Q. Reactivation of spent catalytic cracking catalysts. Master's Thesis, China University of Petroleum (EastChina), China, 2018 (in Chinese). 张景琪. 催化裂化废催化剂的复活. 硕士学位论文, 中国石油大学(华东), 2018. 11 Liu X M, Zhang X G, Pan Z H, et al. Petroleum Processing and Petrochemicals, 2006, 37(11), 44 (in Chinese). 刘欣梅, 张新功, 潘正鸿, 等. 石油炼制与化工, 2006, 37(11), 44. 12 Li C Y, Sha Y X, Gu Y P, et al. Journal of China University of Petro-leum(Edition of Natural Science), 2005, 29(4), 115 (in Chinese). 李春义, 沙有鑫, 顾艳萍, 等. 中国石油大学学报(自然科学版), 2005, 29(4), 115. 13 Cho S I, Jung K S, Woo S I. Applied Catalysis B: Environmental, 2001, 33(3), 249. 14 Tian H. Studies on vanadium removal and rejuvenation of spent FCC catalysts.Master's Thesis, China University of Petroleum (East China), China, 2005 (in Chinese). 田华. 废FCC催化剂脱钒复活研究. 硕士学位论文, 中国石油大学(华东), 2005. 15 Le T Q X, Wang Q, Ravindra A V, et al. Journal of Alloys and Compounds, 2019, 776, 437. 16 Chang J, Zhang E D, Zhang L B, et al. Ultrasonics Sonochemistry, 2017, 34, 222. 17 Liao T Q, Xi Y H, Zhang L B, et al. Journal of Hazardous Materials, 2021, 408, 124464. 18 Zhang C, Liu J H, Yang X B, et al. Journal of Functional Materials, 2015, 46(20), 20063 (in Chinese). 张琛, 刘建华, 杨晓博, 等. 功能材料, 2015, 46(20), 20063. 19 Oza R, Shah N, Patel S. Journal of Chemical Technology & Biotechnology, 2011, 86(10), 1276. 20 Yamashita T, Hayes P. Applied Surface Science, 2008, 254(8), 2441. 21 Chen C M, Yu J, Yoza B A, et al. Journal of Environmental Management, 2015, 152, 58. 22 John F M, William F S, Peter E S, et al. Handbook of X-ray photoelectron spectroscopy, physical electronics, MN, America, 1992, pp. 230. 23 Chen J Y, Liu Z Q, Chen H J, et al. Materials Research and Application, 2007, 1(2), 136 (in Chinese). 陈敬阳, 刘志强, 陈怀杰, 等. 材料研究与应用, 2007, 1(2), 136. 24 Beuther H, Flinn R A. Industrial & Engineering Chemistry Product Research & Development, 1963, 2(1), 53. 25 Goel S, Gautam A. Hydrometallurgy, 2010, 101(3-4), 120. 26 Wu Y, Zhang G J, Zhang X G, et al. Petroleum Refinery Engineering, 2011, 41(11), 32 (in Chinese). 吴聿, 张国静, 张新功,等. 炼油技术与工程, 2011, 41(11), 32. 27 Yan J W, Pan D A, Li B. The Chinese Journal of Process Engineering, 2020, 20(11), 1241 (in Chinese). 焉杰文,潘德安,李彬. 过程工程学报, 2020, 20(11), 1241. 28 Jiang F, Chen Y Q, Ju S H, et al. Ultrasonics Sonochemistry, 2018, 48, 88. 29 Xiao J, Yuan J, Tian Z L, et al. Ultrasonics Sonochemistry, 2018, 40, 21. 30 Xie F C, Li H Y, Ma Y, et al. Journal of Hazardous Materials, 2009, 170(1), 430. 31 Yang J H, He L H, Liu X H, et al. Transactions of Nonferrous Metals Society of China, 2018, 28(4), 775.