這個實驗的部分是探討乙酸正丁酯-正丁醇-水 三成份系統受到不同種類的鹽類而產生鹽析效應的影響,因此在此25℃下,用乙酸正丁酯-正丁醇-水所設計的系統,分別加入飽和磷酸鈉、磷酸氫鈉濃度下,進行液液平衡實驗得到各成份的莫耳分率。由實驗結果得到的液液平衡相圖中,兩相的不互溶區很明顯的變大了,並發現此兩種鹽產生的鹽析效應的大小關聯性。 這個理論的部分以 TTK - Wilson 活性係數模式來描述溶液到底有多偏離理想溶液,為了模擬鹽效應在混合溶劑系統之液液平衡,以TTK-Wilson活性係數模式作理論模擬結果與實驗的結果相符合。
In chemical industry, separation processing is usually considered as a useful technology for the optimal design of unit operation and processing. Adding diverse electrolytes (salts) with different amounts can separate the mixture, n-Butyl Acetate-n-Butanol-water, in esterification through salting analysis processing. The ester type of products with a higher purity can be produced or designated for further purification processing. This research is consisted of experimental and theoretical investigations. In the experimental part, the salting analysis processing in a mixture of n-Butyl Acetate-n-Butanol-water under temperature 25℃ is individually performed with two salts, sodium phosphate and sodium phosphate dibasic.The equilibrium charts of liquid-liquid phase analyzed from the experimental results show that an extending non-dissolution area for two solvents is obviously found after adding salts.The results also reflect the same trend occurring at a decreasing solubility for both n-Butyl Acetate-water and n-Butanol-water. The effect of salting analysis processing deceases in the order of sodium phosphate and sodium phosphate dibasic. To simulate the liquid-liquid phase equilibrium in mixing solvents, the TTK - Wilson activity coefficient model is adopted to describe the deviation between the ideal solvent and the solvent in our research. By computing the liquid-liquid phase equilibrium of electrolytes in mixing solvents, the experimental results show a high degree of consistence, an average deviation of less than 0.8%, with theoretical prediction.