Terdale Santosh S, Dagade Dilip H, Patil Kesharsingh J
Department of Chemistry, Shivaji University, Kolhapur-416 004, India.
J Phys Chem B. 2006 Sep 21;110(37):18583-93. doi: 10.1021/jp063684r.
Osmotic vapor pressure and density measurements were made for aqueous alpha-cyclodextrin (alpha-CD) solutions in the temperature range between 293.15 and 313.15 K. The experimental osmotic coefficient data were used to determine the corresponding activity coefficients and the excess Gibbs free energy of solutions. Further, the activity data obtained at different temperatures along with the enthalpies of dissolution (reported in the literature) were processed to obtain the excess enthalpy and excess entropy values for the solution process. The partial molar entropies of water and of alpha-cyclodextrin were calculated at different temperatures and also at different concentrations of alpha-CD. Using the partial molar volume data at infinite dilution, the solute-solvent cluster integrals were evaluated which yielded information about solute-solvent interactions. The application of McMillan-Mayer theory of solutions was made to obtain osmotic second and third virial coefficients which were decomposed into attractive and repulsive contributions to solute-solute interactions. The second and third osmotic virial coefficients are positive and show minimum at 303.15 K. The Kirkwood-Buff (KB) integrals G(ij), defined by the equation G(ij) = f(infinity)0 (g(ij)- 1)4pir(2) dr, have been evaluated using the experimental osmotic coefficient (and hence activity coefficient) and partial molar volume data. The limiting values of KB integrals, G(ij)(0) are compared with molecular interaction parameters (solute-solute i.e., osmotic second virial coefficient) obtained using McMillan-Mayer theory of solutions. We found an excellent agreement between the two approaches.
在293.15至313.15 K的温度范围内,对α-环糊精(α-CD)水溶液进行了渗透压和密度测量。实验得到的渗透系数数据用于确定相应的活度系数和溶液的过量吉布斯自由能。此外,将不同温度下获得的活度数据与溶解焓(文献报道)一起处理,以获得溶液过程的过量焓和过量熵值。计算了不同温度以及不同α-CD浓度下,水和α-环糊精的偏摩尔熵。利用无限稀释下的偏摩尔体积数据,评估了溶质-溶剂簇积分,从而得到有关溶质-溶剂相互作用的信息。应用麦克米兰-迈耶溶液理论获得了渗透压第二和第三维里系数,并将其分解为溶质-溶质相互作用的吸引和排斥贡献。第二和第三渗透压维里系数为正值,且在303.15 K时显示出最小值。通过实验得到的渗透系数(进而得到活度系数)和偏摩尔体积数据,计算了由方程G(ij) = f(infinity)0 (g(ij)- 1)4pir(2) dr定义的柯克伍德-布夫(KB)积分G(ij)。将KB积分的极限值G(ij)(0)与使用麦克米兰-迈耶溶液理论获得的分子相互作用参数(溶质-溶质,即渗透压第二维里系数)进行了比较。我们发现这两种方法之间有很好的一致性。