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Experimental studies on Thermal and Catalytic slow pyrolysis of groundnut shell to Pyrolytic oil

机译:热解壳热催化慢热解的试验研究热解油

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Pyrolysis process in a fixed bed reactor was performed to derive pyrolytic oil from groundnut shell. Experiments were conducted with different operating parameters to establish optimum conditions with respect to maximum pyrolytic oil yield. Pyrolysis process was carried out without catalyst (thermal pyrolysis) and with catalyst (catalytic pyrolysis). The Kaolin is used as a catalyst for this study. The maximum pyrolytic oil yield (39%wt) was obtained at 450°C temperature for 1.18-2.36 mm of particle size and heating rate of 60°C/min. The properties of pyrolytic oil obtained by thermal and catalytic pyrolysis were characterized through Fourier Transform Infrared Spectroscopy (FT-IR) and Gas Chromatography-Mass Spectrometry (GC-MS) techniques to identify the functional groups and chemical components present in the pyrolytic oil. The study found that catalytic pyrolysis produce more pyrolytic oil yield and improve the pH value, viscosity and calorific value of the pyrolytic oil as compared to thermal pyrolysis.
机译:进行固定床反应器中的热解过程以从地下壳中衍生热解油。用不同的操作参数进行实验,以确定相对于最大热解油产量的最佳条件。无需催化剂(热热解)和催化剂(催化热解)进行热解过程。高岭土用作本研究的催化剂。在450℃温度下获得最大热解油产率(39%WT),粒度为1.18-2.36mm,加热速率为60℃/ min。通过傅里叶变换红外光谱(FT-IR)和气相色谱 - 质谱(GC-MS)技术表征通过热和催化热解的热解油的性质,以鉴定热解油中存在的官能团和化学成分。该研究发现,与热热解相比,催化热解产生更多的热解油产生并改善热解油的pH值,粘度和热值。

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