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Study on the Elution Ability of Salicylic acid in Supercritical Carbon Dioxide

机译:超临界二氧化碳中水杨酸洗脱能力的研究

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The elution ability of salicylic acid on ion exchange resins in supercritical carbon dioxide has been studied. Some factors influencing elution recovery, including entrainer, temperature, pressure, flow rate of supercritical fluid CO2 are discussed in this work. The addition of small amount of entrainer, such as ethanol, triethanolamine and their mixture to supercritical CO2 can cause dramatic effects on the elution ability. The results show that the salicylic acid can be only slightly eluted from the resin with supercritical CO2 alone with temperatures ranging from 307.15 to 323.15K and pressures ranging from 10 to 30MPa. Meanwhile, with the same T, P conditions, 40.58%, 73.08% salicylic acid can be eluted from the ion exchange resin with ethanol and ethanol+triethanolamine as the entrainer, respectively. An improved PR equation of state with VDW1 mixing rules is used to calculate the elution recovery of salicylic acid in supercritical CO2 and the results agree well with the experimental data.
机译:研究了水杨酸在超临界二氧化碳中的离子交换树脂上的洗脱能力。在这项工作中讨论了一些影响洗脱回收的因素,包括夹带剂,温度,压力,流速CO2的流速。向超临界CO 2中添加少量夹带剂,例如乙醇,三乙醇胺及其混合物会对洗脱能力产生显着的影响。结果表明,水杨酸只能用超临界CO2轻微洗脱,单独使用307.15至323.15K的温度和10至30MPa的压力。同时,具有相同的T,P载体,40.58%,73.08%的水杨酸可以分别用乙醇和乙醇+三乙醇胺作为夹带剂从离子交换树脂中洗脱。具有VDW1混合规则的改进的状态方程用于计算超临界CO2中水杨酸的洗脱回收,结果与实验数据很好。

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