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在流动酶整体式反应器中水中四环素的降解的实验和模拟。

Experimental and modeling of tetracycline degradation in water in a flow-through enzymatic monolithic reactor.

机构信息

Institut Européen des Membranes, Univ Montpellier, CNRS, ENSCM, Montpellier, France.

Institut Charles Gerhardt Montpellier, Univ Montpellier, CNRS, ENSCM, Montpellier, France.

出版信息

Environ Sci Pollut Res Int. 2022 Oct;29(50):75896-75906. doi: 10.1007/s11356-022-21204-y. Epub 2022 Jun 4.

Abstract

In this work, the laccase from Trametes versicolor was immobilized in highly porous silica monoliths (0.6-cm diameter, 0.5-cm length). These monoliths feature a unique homogeneous network of interconnected macropores (20 μm) with mesopores (20 nm) in the skeleton and a high specific surface area (330 m/g). The enzymatic monoliths were applied to degrade tetracycline (TC) in model aqueous solutions (20 ppm). For this purpose, a tubular flow-through reactor (FTR) configuration with recycling was built. The TC degradation was improved with oxygen saturation, presence of degradation products, and recirculation rate. The TC depletion reaches 50% in the FTR and 90% in a stirred tank reactor (CSTR) using crushed monoliths. These results indicate the importance of maintaining a high co-substrate concentration near active sites. A model coupling mass transfers with a Michaelis-Menten kinetics was applied to simulate the TC degradation in real wastewaters at actual TC concentration (2.8 10 ppm). Simulation results show that industrial scale FTR reactor should be suitable to degrade 90% of TC in 5 h at a flow rate of 1 mL/min in a single passage flow configuration. Nevertheless, the process could certainly be further optimized in terms of laccase activity, oxygen supply near active sites, and contact time.

摘要

在这项工作中,来自变色栓菌的漆酶被固定在高度多孔的硅质整体式(直径 0.6 厘米,长 0.5 厘米)中。这些整体式具有独特的均匀互连大孔网络(20 μm),骨架中有中孔(20nm),并且具有高比表面积(330 m/g)。将酶促整体式应用于在模型水溶液(20 ppm)中降解四环素(TC)。为此,构建了带有循环的管状流动式反应器(FTR)配置。通过氧气饱和、降解产物的存在和再循环速率提高了 TC 的降解。在 FTR 中,TC 的消耗达到 50%,在使用碎整体式的搅拌槽反应器(CSTR)中达到 90%。这些结果表明,在活性位点附近保持高共底物浓度非常重要。应用耦合传质与米氏动力学的模型来模拟实际 TC 浓度(2.8×10 ppm)下实际废水中的 TC 降解。模拟结果表明,在单通道流动配置下,工业规模的 FTR 反应器应该适合在 5 小时内以 1 mL/min 的流速将 90%的 TC 降解。然而,在漆酶活性、活性位点附近的氧气供应和接触时间方面,该过程肯定可以进一步优化。

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