钾盐
硫酸钾
结晶
相图
等温过程
硫酸铵
镁
钾
溶解
化学
盐(化学)
硫酸盐
铵
矿物学
分析化学(期刊)
相(物质)
无机化学
热力学
物理化学
有机化学
物理
作者
Cheng Li,Xueqing Chen,Hongfei Guo,Xue Zhou,Jilin Cao
标识
DOI:10.1111/1755-6724.14409
摘要
Abstract Based on the requirement of the new technology for producing potassium sulfate and N‐Mg compound fertilizer, boussingaultite, by the reaction of the mineral shoenite from Kunteyi Salt Lake, Qinghai province, and the industrial byproduct ammonium sulfate, the solubilities of the quaternary system (NH 4 ) 2 SO 4 ‐MgSO 4 ‐K 2 SO 4 ‐H 2 O at 25.0°C in the isothermal evaporation and crystallization process were measured using the isothermal evaporation method, and the corresponding phase diagrams were plotted. According to the diagram, this system contains six saturation points and six solid phase fields of crystallization, which correspond to (K 1‐m ,(NH 4 ) m ) 2 SO 4 , (NH 4 ) 2 SO 4 ·MgSO 4 ·6H 2 O, K 2 SO 4 ·MgSO 4 ·6H 2 O, MgSO 4 ·6H 2 O, (K 1‐n ,(NH 4 ) n ) 2 SO 4 ·MgSO 4 ·6H 2 O and MgSO 4 ·7H 2 O, respectively. By analyzing and calculating the isothermal evaporation and dissolution phase diagram of this quaternary system at 25.0°C, K 2 SO 4 and (NH 4 ) 2 SO 4 ·MgSO 4 ·6H 2 O can be separated via K 2 SO 4 ·MgSO 4 ·6H 2 O and (NH 4 ) 2 SO 4 as raw materials. Theoretical calculations about the proposed process were carried out and verified by experiment, which indicated that the yield of potassium sulfate was improved and the magnesium resources were fully utilized.
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