Zabaniotou A, Stavropoulos G, Skoulou V
Department of Chemical Engineering, Aristotle University of Thessaloniki, University Campus, Thessaloniki, Greece.
Bioresour Technol. 2008 Jan;99(2):320-6. doi: 10.1016/j.biortech.2006.12.020. Epub 2007 Feb 20.
Activated carbons have been prepared from olive kernels and their adsorptive characteristics were investigated. A two stage process of pyrolysis-activation has been tested in two scales: (a) laboratory scale pyrolysis and chemical activation with KOH and (b) pilot/bench scale pyrolysis and physical activation with H(2)O-CO(2). In the second case, olive kernels were first pyrolysed at 800 degrees C, during 45 min under an inert atmosphere in an industrial pyrolyser with a throughput of 1t/h (Compact Power Ltd., Bristol, UK). The resulting chars were subsequently activated with steam and carbon dioxide mixtures at 970 degrees C in a batch pilot monohearth reactor at NESA facility (Louvain-la Neuve, Belgium). The active carbons obtained from both scales were characterized by N(2) adsorption at 77 K, methyl-blue adsorption (MB adsorption) at room temperature and SEM analysis. Surface area and MB adsorption were found to increase with the degree of burn-off. The maximum BET surface area was found to be around 1000-1200 m(2)/g for active carbons produced at industrial scale with physical activation, and 3049 m(2)/g for active carbons produced at laboratory with KOH activation. The pores of the produced carbons were composed of micropores at the early stages of activation and both micropores and mesopores at the late stages. Methylene blue removal capacity appeared to be comparable to that of commercial carbons and even higher at high degrees of activation.
已用橄榄核制备了活性炭,并对其吸附特性进行了研究。在两个规模上测试了热解 - 活化的两阶段过程:(a) 实验室规模的热解和用氢氧化钾进行化学活化,以及 (b) 中试/试验规模的热解和用H₂O - CO₂进行物理活化。在第二种情况下,橄榄核首先在800℃下于工业热解器中在惰性气氛下热解45分钟,该热解器的产量为1吨/小时(英国布里斯托尔的Compact Power Ltd.)。随后在NESA设施(比利时鲁汶新镇)的间歇式中试单炉膛反应器中,在970℃下用蒸汽和二氧化碳混合物对所得炭进行活化。从两个规模获得的活性炭通过在77K下的N₂吸附、室温下的亚甲基蓝吸附(MB吸附)和扫描电子显微镜分析进行表征。发现比表面积和MB吸附随烧失程度增加。对于通过物理活化在工业规模生产的活性炭,最大BET比表面积约为1000 - 1200 m²/g,而对于在实验室用氢氧化钾活化生产的活性炭,最大BET比表面积为3049 m²/g。所生产的炭的孔在活化早期由微孔组成,在后期由微孔和中孔组成。亚甲基蓝去除能力似乎与商业活性炭相当,在高活化程度下甚至更高。