Production of high purity MoO3 3 from spent catalyst of formaldehyde synthesis process via a novel two-step leaching-cementation method

被引:2
作者
Mohammadi, Sajjad [1 ]
Najafabadi, Ali Taheri [1 ]
Aboody, Hossein [1 ]
Akhlaghi, Mohammad Reza [1 ]
Saidi, Majid [1 ]
机构
[1] Univ Tehran, Coll Sci, Sch Chem, POB 14155-6455, Tehran, Iran
关键词
Spent formaldehyde synthesis catalyst; FORMOX process; Alkaline leaching; Design of experiment (DOE); Zn cementation; MoO; 3; synthesis; HYDRODESULFURIZATION CATALYSTS; VALUABLE METALS; SELECTIVE RECOVERY; MOLYBDENUM; VANADIUM; EXTRACTION; NICKEL; OXIDATION; REMOVAL; ACID;
D O I
10.1016/j.jiec.2024.03.044
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
This study presents a two-step methodology for producing high-purity MoO3 3 from spent FORMOX process catalysts. In the first step, a leaching process with a Na2CO3 2 CO 3 solution is used to get molybdenum out of formaldehyde synthesis catalyst. The second step involves molybdenum-ion cementation in the presence of metallic zinc powder and plates. The leaching process is thoroughly explored using the design of experiments (DOE) to analyze critical parameters such as temperature, leaching time, Na2CO3/Mo 2 CO 3 /Mo stoichiometric ratio, and catalyst average particle size. A robust quadratic model with an R2 2 value exceeding 97 % is developed, serving as a predictive tool for molybdenum extraction. Through rigorous numerical optimization, the optimal conditions for 100 % extraction were found to be 74.5 degrees C, 92.3 min, a stoichiometric ratio of 2.52, and a particle size of 183 mu m. However, the use of zinc powder in the cementation stage introduces impurities due to increased solution pH and reduced zinc dissolution. The strategic adoption of zinc plates mitigates these challenges, resulting in a notable enhancement of the final product's purity. Over 91 % of MoO4-2 4-2 ions with a purity surpassing 99.8 % are successfully obtained as hexagonal MoO3 3 powder at 85 degrees C with an initial solution pH of 1.0 after 15 min of the cementation process.
引用
收藏
页码:559 / 571
页数:13
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