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昆明冶金职业大学学报 ›› 2026, Vol. 42 ›› Issue (3): 27-.DOI: 10.3969/j.issn.1009-0479.2026.03.004

• 环境保护与化工技术 • 上一篇    下一篇

pH 值对烧结烟气氨法脱硫硫酸铵结晶影响

  

  1. (1. 武钢集团昆明钢铁股份有限公司,云南安宁 650302;2. 云南天朗节能环保集团有限公司,云南安宁 650302;3. 昆明理工大学冶金与能源工程学院,云南昆明 650093)
  • 出版日期:2026-08-31 发布日期:2026-09-01
  • 作者简介:袁晓红(1991-)女,云南南华人,工程师,理学硕士,主要从事化学分析与环境科学研究。

The Influence of pH on Ammonia Sulfate Crystallization in the Flue Gas Desulfurization Process

  1. (1. Wugang Group Kunming Iron and Steel Co., Ltd., Anning 650302, Yunnan, China; 2. Yunnan Tianlang Energy Conservation and Environmental Protection Group Co., Ltd., Anning 650302, Yunnan, China; 3. Faculty of Metallurgical and Energy Engineering, Kunming University of Science and Technology, Kunming 650093, China)
  • Online:2026-08-31 Published:2026-09-01

摘要: 昆钢新区脱硫系统由于烧结烟气携带大量杂质,导致硫酸铵结晶差甚至不结晶,严重影响昆钢新区脱硫系统的稳定生产。为探明 pH 值对硫酸铵结晶的影响,分别采用 NaOH、Ca (OH)₂、Na₂CO₃和 CaCO₃调节硫酸铵一效溶液 pH 值,探究 pH 对蒸发结晶量与增产率的变化规律;采用硫酸与氨水调控硫酸铵二效溶液 pH 值,分析冷却结晶条件下 pH 对结晶产量、晶体平均粒径及变异系数的影响。试验结果表明:以 NaOH 将一效硫酸铵溶液 pH 调节至约 5.25 后蒸发浓缩结晶,可得到 63.493 g 硫酸铵晶体,且 NaOH 消耗量最低,仅为 0.283 g;二效硫酸铵溶液的最优 pH 为 2.5,该工况下获得 61.162 g 硫酸铵产品,晶体颗粒更大、粒度分布均匀,晶形规整,杂质含量低,与纯硫酸铵晶体形貌接近。该研究结果可为昆钢新区硫酸铵结晶工艺优化、提升硫酸铵产量提供理论依据。

关键词: 氨法脱硫, 硫酸铵, 蒸发结晶, 冷却结晶

Abstract: Due to numerous impurities carried by sintering flue gas, ammonium sulfate crystallization becomes poor or even fails to occur, which hinders the stable production of the desulfurization system in the new area of Kunming Iron and Steel. To investigate the effect of pH on ammonium sulfate crystallization, NaOH, Ca(OH)₂, Na₂CO₃ and CaCO₃ were adopted to adjust the pH of the first‑effect ammonium sulfate solution, and the influences of pH on crystallization mass and yield‑increase ratio were studied. Sulfuric acid and ammonia water were used to regulate the pH of the second‑effect ammonium sulfate solution, and the effects of pH on crystallization yield, average particle size and coefficient of variation were explored. The results show that when the pH of the first‑effect ammonium sulfate solution is adjusted to approximately 5.25 with NaOH before evaporation, concentration and crystallization, a high ammonium sulfate yield of 63.493 g can be obtained with the minimum NaOH dosage of 0.283 g. The optimal pH for the second‑effect ammonium sulfate solution is 2.5. Under this condition, 61.162 g of ammonium sulfate crystals with large particle size, uniform particle distribution, regular morphology and low impurity content can be obtained, and the crystal morphology is highly consistent with pure ammonium sulfate. These findings can provide a reference for optimizing the crystallization process and increasing the output of ammonium sulfate.

Key words: ammonia process of desulfurization, ammonium sulfate, evaporative crystallization, cooling crystallization

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