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Design and operation of an inexpensive, laboratory-scale, continuous hydrothermal liquefaction reactor for the conversion of microalgae produced during wastewater treatment

机译:设计和运行廉价的实验室规模的连续水热液化反应器,用于转化废水处理过程中产生的微藻

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摘要

Recently, much research has been published on the hydrothermal liquefaction (HTL) of microalgae to form bio-crude, which can be further upgraded into sustainable 3rd generation biofuels. However, most of these studies have been conducted in batch reactors, which are not fully applicable to large-scale industrial production. In this investigation an inexpensive laboratory scale continuous flow system was designed and tested for the liquefaction of microalgae produced during wastewater treatment. The system was operated at a range of temperatures (300 °C–340 °C) and flow rates (3–7 mL min− 1), with the feed being delivered using high pressure N2 rather than a mechanical pump. The design incorporated the in-situ collection of solids through a double tube design. The algae was processed at 5 wt% and the results were compared to those from a batch reactor operated at equivalent conditions. By combining high heating rates with extended reaction times, the continuous system was able to yield significantly enhanced bio-crude yields compared to the batch system. This demonstrates the need for inexpensive continuous processing in the lab, to aid in scale up decision making.
机译:最近,关于微藻的水热液化(HTL)形成生物原油的大量研究已经发表,可以进一步升级为可持续的第三代生物燃料。但是,这些研究大多数是在间歇式反应器中进行的,不适用于大规模工业生产。在这项研究中,设计并测试了一种廉价的实验室规模连续流系统,用于废水处理过程中产生的微藻的液化。该系统在一定温度范围(300°C–340°C)和流速(3–7 mL min-1)下运行,进料使用高压N2而不是机械泵输送。该设计通过双管设计结合了固体的原位收集。将藻类以5 wt%进行处理,并将结果与​​在相同条件下运行的间歇式反应器的结果进行比较。通过将高加热速率与延长的反应时间相结合,与分批系统相比,连续系统能够显着提高生物粗品的产量。这表明需要在实验室中进行廉价的连续处理,以帮助扩大决策范围。

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