镍铈/HZSM-5催化剂催化蔗渣热解的热重动力学研究

V. Balasundram, Khairunnisa Kamarul Zaman, Norazana Ibrahim, R. Kasmani, R. Isha, M. Hamid, H. Hasbullah
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引用次数: 4

摘要

摘要本研究旨在研究镍铈/HZSM-5催化剂对甘蔗渣热解的影响,并通过热重分析仪对其进行动力学分析。样品在氮气环境中以多种加热速率(5,10,20和30°C/min)从30°C热解至700°C。以HZSM-5为载体,采用初湿浸渍法浸渍镍和铈作为促进剂。对于催化样品,催化剂与生物质的比例固定为1:1。采用Flynn-Wall-Ozawa和Coats-Redfern方法对非催化和催化热解进行了动力学分析。采用Flynn-Wall-Ozawa方法,催化热解的转化率活化能(2.87 ~ 68.92 kJ/mol)高于非催化热解的转化率活化能(24.20 ~ 122.33 kJ/mol)。通过Coats-Redfern,非催化热解和催化热解的反应机理分别遵循幂定律(n=1)和化学反应(n=2)
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Thermogravimetric Kinetics of Catalytic Pyrolysis of Sugarcane Bagasse over Nickel-Cerium/HZSM-5 Catalyst
Malaysia ABSTRACT The objective of this research is to investigate the performance of Nickel-Cerium/HZSM-5 catalyst on pyrolysis of sugarcane bagasse and kinetic analysis via thermogravimetric analyzer. The sample is pyrolyzed from 30 to 700 °C at multiple heating rates (5, 10, 20, and 30 °C/min) in a nitrogen environment. The HZSM-5 was used as a support, while nickel and cerium were impregnated as promoters via incipient wetness impregnation method. For catalytic samples, the catalyst to biomass ratio was fixed at 1:1. The kinetic analysis of non-catalytic and catalytic pyrolysis was performed using the Flynn-Wall-Ozawa and Coats-Redfern methods. The catalytic pyrolysis has achieved higher activation energy (2.87 – 68.92 kJ/mol) over conversion than the non-catalytic pyrolysis (24.20 – 122.33 kJ/mol) using the Flynn-Wall-Ozawa method. The reaction mechanism of non-catalytic and catalytic pyrolysis follows power law (n=1) and chemical reaction (n=2) respectively via the Coats-Redfern
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