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A Continuous Extraction and Pumpless Supercritical CO 2 Drying System for Laboratory-Scale Aerogel Production

机译:用于实验室规模气凝胶生产的连续萃取和无泵超临界CO 2干燥系统

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Production of aerogels starts with solution chemistry and may end with supercritical carbon dioxide drying, which both require a specialized system. Here we present a complete aerogel production system that was developed and used in our laboratory over the last nine years. Our aim was to develop a supercritical dryer and a protocol, whereby the CO 2 pump can be left out, and the entire flow system is operated by the pressure of the CO 2 cylinder. Drying pressure and temperature are controlled by the combination of the filling and heating temperatures. A continuous-mode solvent exchange system has also been developed, in which the solvent consumption during the process can be reduced to one-third of the batch method. In the new medium temperature 1.5 L volume supercritical dryer, the temperature is set to a constant 80–82 °C, and the pressure can be in the 90–200 bar range, depending on the conditions. We have performed approximately 200 dryings thus far, and prepared a wide range of monolithic aerogels, from pristine silica aerogels to polysaccharides and collagen. In this paper, we have summarized not only the technical details, but also the work experiences, as well as advantages and disadvantages of the systems.
机译:气凝胶的生产从溶液化学开始,并可能以超临界二氧化碳干燥结束,这两者都需要专门的系统。在这里,我们介绍了完整的气凝胶生产系统,该系统在过去的九年中一直在我们的实验室中开发和使用。我们的目标是开发一种超临界干燥机和规程,从而可以省去CO 2泵,并且整个流动系统都通过CO 2气瓶的压力进行操作。干燥压力和温度由填充温度和加热温度共同控制。还开发了一种连续模式的溶剂交换系统,在该系统中,该过程中的溶剂消耗可以减少到间歇方法的三分之一。在新的中温1.5 L容积超临界干燥机中,温度设置为恒定80-82°C,压力可以在90-200 bar范围内,具体取决于条件。到目前为止,我们已经进行了约200次干燥,并准备了从原始二氧化硅气凝胶到多糖和胶原蛋白的各种整体式气凝胶。在本文中,我们不仅总结了技术细节,还总结了系统的工作经验以及优缺点。

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