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Design of Supercritical Fluid Extractor Using Dry Ice as A Supercritical Solvent

机译:用干冰作为超临界溶剂的超临界流体提取器设计

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The supercritical fluid extraction is the most effective and efficient way to extract valuable constituent in botanicals but the apparatus is usually very complex, complicated and expensive. Carbon dioxide gas needs to be pumped and pressed to reach its supercritical pressure. In this research, the supercritical CO_2 condition was achieved by sublimation of a certain amount of dry ice (CO_2 solid). The achieved pressure depends on the mass of dry ice. By developing supercritical extraction technology using this dry ice, the apparatus becomes simpler so the price becomes less expensive. Since this method is also able to be operated in a batch operation, the equilibrium data could be obtained. The objective of this research was to design of supercritical fluid extraction apparatus using dry ice as a supercritical solvent. The designed apparatus consisted of 2 main vessels. The first one was a high-pressure extractor for extracting process using supercritical CO_2 solvent. The second one was a separator vessel for separating solvent and extract. During the experiment, the gas leakage of the high-pressure apparatus often occurred. To avoid the leakage, the valves and pipes used the standard brands of Swagelok and Sanvik. Similarly, the design of extractor cover used o ring with silicone rubber material. The leakage that occurred during high-pressure operations was very dangerous. To ensure safety, installation of series of apparatus was covered by perforated iron with 2 pieces of windows made of an acrylic material to facilitate in monitoring the process. In this research, the correlation of the dry ice mass and the achieved pressure at a temperature of 40 °C was also studied. The Equation of State (EOS), such as Ideal Gas, van der Waals, Redlich Kwong, Soave-Redlich Kwong, and Peng Robinson were explored to predict the operating condition (supercritical pressure and temperature). By comparing the calculated pressure at various Equation of State and the experimental da
机译:超临界流体提取是提取植物中有价值的成分的最有效和有效的方法,但该装置通常非常复杂,复杂且昂贵。需要泵送二氧化碳气体并压制以达到其超临界压力。在该研究中,通过升华一定量的干冰(CO_2固体)来实现超临界CO_2条件。实现的压力取决于干冰的质量。通过开发使用该干冰的超临界提取技术,该装置变得更简单,因此价格变得不那么昂贵。由于该方法也能够在批量操作中操作,因此可以获得平衡数据。本研究的目的是设计使用干冰作为超临界溶剂的超临界流体提取装置。设计的装置由2个主体组成。第一个是用于使用超临界CO_2溶剂提取过程的高压提取器。第二个是用于分离溶剂和提取物的分离器容器。在实验期间,经常发生高压装置的气体泄漏。为避免泄漏,阀门和管道使用了Swagelok和Sanvik的标准品牌。类似地,用硅橡胶材料的萃取器盖的设计设计。高压操作期间发生的泄漏非常危险。为确保安全性,通过穿孔铁覆盖一系列设备的安装,其中2件窗户由丙烯酸材料制成,以便于监测该过程。在该研究中,还研究了干冰质量和在40℃的温度下实现的压力的相关性。探讨了国家(EOS)的等式,例如理想的天然气,van der Waals,Redlich Kwong,Soave-Redlich Kwong和Peng Robinson,以预测操作条件(超临界压力和温度)。通过将计算的压力与各个状态等方程的比较和实验DA进行比较

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