کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
212059 462031 2015 13 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Synthesis of hydrometallurgical processes for valorization of secondary raw materials using ant colony optimization and key performance indicators
ترجمه فارسی عنوان
سنتز فرایندهای هیدرومغناطیسی برای ارزش گذاری مواد خام ثانویه با استفاده از بهینه سازی کلزا و شاخص های عملکرد کلیدی
کلمات کلیدی
سنتز فرایند، توسعه فرایند، بهینه سازی کلینیک مورچه، درمان گرد و غبار، عناصر نادر زمین
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
چکیده انگلیسی


• Method for synthesis of hydrometallurgical processes with limited amount of experimental data.
• Key performance indicators characterize purification performance and costs.
• The stochastic method offers significantly reduced computation times.

An algorithm-based method for synthesis of hydrometallurgical processes using limited amounts of experimental data is presented. The method enables simultaneous selection and sequencing of unit operations and optimization of operating parameters. An ant colony optimization (ACO) based algorithm is used to identify the most economic process alternative in an iterative manner. Key performance indicators are used for comparison of candidate processes: a purification performance index measures purity improvement and a separation cost indicator is used as an objective function in process optimization. Computational times were reduced significantly with the suggested method compared to an algorithm which evaluates all the possible process options. The practical applicability of the method to hydrometallurgy is demonstrated by investigating zinc recovery from argon oxygen decarburization dust with two alternative leaching methods and recovery of lanthanides from nickel metal hydride (NiMH) batteries. In the first zinc recovery process, 150 min normal batch leaching with 0.5 M H2SO4 is used, and in the other one 270 min batch leaching with H2SO4 is done by controlling the pH (> 3.0). In both cases the leachate is extracted with D2EHPA at pH 4.27, and stripped with circulating solution from zinc electrolysis. For lanthanides recovery the algorithm suggested a process in which the raw material is leached with 1.3 M HCl, the leachate is extracted with D2EHPA at pH 2.2, organic phase is stripped with 2.0 M HCl and 99% pure Ln-oxalates are precipitated with oxalic acid at pH 0.6. Compared to previously suggested process for the same raw material, the algorithm suggests operating the leaching step such that higher selectivity is achieved by sacrificing some yield.

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ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Hydrometallurgy - Volume 153, March 2015, Pages 121–133
نویسندگان
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