钢铁企业富钾烧结电除尘灰水浸液经脱除重金属杂质后可看作四元水盐体系KCl-NaCl-CaCl2-H2O,从该体系分离出氯化钾,需要首先通过蒸发浓缩及蒸发结晶。为了合理有效的控制蒸发操作过程,今采用静态法实验测定了四元水盐体系KCl-NaCl-CaCl2-H2O在KCl浓度为0～3 mol L 1,NaCl浓度为0～2 mol L 1,CaCl2浓度为0～1 mol L 1,温度为303.15～373.15 K的蒸气压,并通过数学线性回归得出了该体系的蒸气压与温度和体系组成的关系式,该关系式的获得有望为实际蒸发操作过程控制提供理论依据。
In order to examine the leaching rate of potassium chloride from the sintering dust by water,surface morphology and inner structure of the dust,especially the existing state of potassium chloride,were observed by scanning electron microscopy（SEM） and linear scanning technique via energy dispersive spectroscopy（EDS）.The characterization shows that the sintering dusts are mostly porous composites or agglomerates of the fine dust particles with size less than 10 μm,and the potassium chloride and sodium chloride particles are partly covered by other water insoluble matters in the dust which consist of elements iron,calcium and etc.Exposure of potassium chloride in the agglomerated dust matrix of this kind suggests that the leaching can be simply perceived as the dissolution of water soluble matters in the dust.On-line monitor of specific electrical conductivity of the leaching system verifies the prediction that leaching kinetics of potassium chloride from the sintering dust fits dissolution model well.Leaching equilibrium can be reached within 5 min with potassium leaching ratio more than 95%.
