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Chemcial Industry and Engineering 2014, Vol. 31 Issue (5) :49-53    DOI: doi: 10.13353/j.issn.1004.9533.2014.05.009
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Solid-Liquid Phase Equilibrium and Phase Diagram for Ternary TheophyllineNicotinamideIsopropanol System at 298.15 and 308.15 K
 GUO  Jing-Jing, DANG  Le-Ping, WEI  Hong-Yuan
(School of Chemical Engineering and Technology, Tianjin University, Tianjin 300072, China)

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Abstract In this paper, the theophylline (TP)-nicotinamide (NCT) cocrystal formed by intermolecular hydrogen bond was used as an example for studying the thermodynamic analysis of cocrystal. The solubility and solubility product (Ksp) of theophyllinenicotinamide cocrystal in isopropanol were measured at 298.15 and 308.15 K at atmospheric pressure. The solubility data shows that significant complexation occurs in some solutions, and the relevant constant K11 is derived. The dependence of cocrystal solubility on the concentration of cocrystal components in solution were measured and explained by a cocrystal solubility product and by the binding constants of complexes formed in solution. The effect of temperature on solubility product and complex constant was also discussed. In order to investigate how the cocrystals crystallized at different temperature, the ternary phase diagrams for theophyllinenicotinamideisopropanol at 298.15 and 308.15 K were constructed and the variation tendency with temperature was discussed. The ternary phase diagrams help us understand how the cocrystal was crystallized from solution and provides theoretical basis for crystallization process.
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GUO Jing-Jing
DANG Le-Ping
WEI Hong-Yuan
Keywords:   
Received 2013-05-20;
Fund:

教育部博士点基金(20110032110022)和天津市自然科学基金(11JCYBJC04600,13JCQNJC05200)。

Corresponding Authors: 党乐平,电话:(022)27400287,E-mail:dleping@163.com。     Email: dleping@163.com
About author: 郭晶晶(1989-),女,硕士研究生,研究方向为药物结晶。
Cite this article:   
GUO Jing-Jing, DANG Le-Ping, WEI Hong-Yuan.Solid-Liquid Phase Equilibrium and Phase Diagram for Ternary TheophyllineNicotinamideIsopropanol System at 298.15 and 308.15 K[J]  Chemcial Industry and Engineering, 2014,V31(5): 49-53
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