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Official PDF TranslationTransactions of Nonferrous Metals Society of China (中国有色金属学报)

CFD modeling of gas−liquid mixing and splashing in industrial-scale bottom-blowing furnace: Effects of melt viscosity

Authors: Cheng-lin LI; You YAN; Ao HAO; Wei-wen HU; Zi-lin YANG; Dong-ling WU; Liu LIU; Hong-jie YAN

DOI: 10.1016/S1003-6326(26)67070-7Status: Verified Translated Edition
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Key Findings in This Report

• • Optimal gas−liquid mixing is achieved at melt viscosities of 0.01 and 0.5 Pa·s, whereas minimal splashing occurs within 0.1−0.25 Pa·s (approximately 1076−1100 °C); this non-overlapping window forces operators to prioritize either mixing or splash suppression, directly affecting reaction completeness and metal recovery. • • Shear stress on the furnace lining increases with melt viscosity and rises particularly rapidly in the 0.1−0.25 Pa·s range, making this interval a critical erosion-risk zone that accelerates refractory wear and shortens campaign life. • • The regions surrounding the oxygen lances are the most susceptible to erosion, identifying localized lance-adjacent refractory as the primary failure point and directing maintenance and design efforts to this area. • • A recommended operating viscosity of 0.01−0.1 Pa·s minimizes erosion while maintaining acceptable mixing, providing a concrete control target for industrial bottom-blowing lead smelting that co-processes lead-containing waste materials.