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Reaction Kinetics and Pathways for Salvianolic Acid B in High Temperature Water

机译:在高温水中的反应动力学和咸酸B的途径

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A kinetic model for the production of salvianolic acid A (Sal A) from salvianolic acid B (Sal B) in high temperaturel water was proposed. The kinetic model includes the following key steps: (1) Sal B hydrolysis and decarboxylation to form salvianolic acid A (Sal A); (2) Sal B reversion/polymization to produce humins (polymerized insoluble carbonaceous species); (3) Sal A cyclization to form Sal C; (4) Sal A degradation to produce humins; (5) Sal C degradation to produce procatechuic aldehyde (PA) and danshensu (DSS). From kinetic analysis, relatively high temperatures are essential for maximum Sal A yield and relatively low temperatures are essential for maximum Sal C yield. The reaction model in this study can be used to predict the optimal production conditions for Sal A in the extraction reaction. Moreover, we also studied the extraction yields of Sal A from Salvia miltiorrhiza Bunge. The results showed that this method was suitable for production of Sal A, but there is no obvious advantage for production of Sal C.
机译:提出了一种在高温水中从咸酸B(SAL B)中生产salvianolic a(sal a)的动力学模型。动力学模型包括以下关键步骤:(1)SAL B水解和脱羧以形成salvianolic Acid A(SAL A); (2)SAL B回归/聚合产生humins(聚合不溶性碳质物种); (3)SAL A环化形成SAL C; (4)降解产生humins的退化; (5)降解产生丙醛醛(PA)和Danshensu(DSS)。从动力学分析中,相对较高的温度对于最大sal a产量至关重要,而相对较低的温度对于最大sal c产量至关重要。这项研究中的反应模型可用于预测提取反应中SAL A的最佳生产条件。此外,我们还研究了Salvia Miltiorrhiza Bunge的Sal A的提取产量。结果表明,该方法适合于生产SAL A,但生产SalC并没有明显的优势。

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