A CaO/zeolite-based catalyst obtained from waste chicken eggshell and coal fly ash for biodiesel production

被引:66
|
作者
Pavlovic, Stefan M. [1 ]
Marinkovic, Dalibor M. [1 ]
Kostic, Milan D. [2 ]
Jankovic-Castvan, Ivona M. [3 ]
Mojovic, Ljiljana, V [3 ]
Stankovic, Miroslav, V [1 ]
Veljkovic, Vlada B. [2 ,4 ]
机构
[1] Univ Belgrade, Inst Chem Technol & Met, Njegoseva 12, Belgrade 11001, Serbia
[2] Univ Nis, Fac Technol, Bulevar Oslobodjenja 124, Leskovac 16000, Serbia
[3] Univ Belgrade, Fac Technol & Met, Karnegijeva 4, Belgrade 11000, Serbia
[4] Serbian Acad Arts & Sci, Knez Mihailova 35, Belgrade 11000, Serbia
关键词
Biodiesel; Fly ash; Zeolitic material; Eggshell; Methanolysis; Kinetic modeling; OF-THE-ART; HETEROGENEOUS CATALYST; SOYBEAN OIL; ZEOLITE; 4A; EGG-SHELL; PALM OIL; TRANSESTERIFICATION; SUNFLOWER; KINETICS; CAO;
D O I
10.1016/j.fuel.2020.117171
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The present paper is focused on the development of a new environment-friendly methanolysis catalyst completely based on waste materials: lignite coal fly ash and chicken eggshells. A novel catalyst based on CaO supported on a fly ash-based zeolitic material (CaO/FA-ZM) was obtained from a cancrinite-sodalite group zeolite-like material (vishnevite type) and active CaO by alkali activation in a new miniature autoclave reactor system and hydration-dehydration. Agitation by rotation of the entire reaction mixture led to a more homogeneous zeolitic product and saved both time and energy. The obtained catalyst structure corresponds to gis-mondine and the crystallographic modification of calcium silicate (alpha'-dicalcium silicate) with deposited CaO. The characteristics of the synthesized catalyst were determined using ED-XRF, XRD, FT-IR, SEM, Hg-porosimetry, N-2-physisorption, LDPSA, and Hammett indicators. The CaO/FA-ZM catalyst exhibited a high activity (97.8% of FAME for only 30 min) and stability (a negligible drop in activity in five consecutive cycles) in the methanolysis reaction under the optimal reaction conditions (temperature of 60 degrees C, methanol/oil molar ratio of 6:1, and catalyst concentration of 6 wt%). A kinetic study was performed using two different mechanisms: the irreversible pseudo-first-order reaction mechanism in two regimes (heterogeneous and homogeneous) and the changing mechanism combined with the triacylglycerol mass transfer limitation. Both models showed a satisfactory agreement between the experimental and predicted values of conversion degree (R-2 > 0.93), confirming their validity for the CaO-based heterogeneously catalyzed methanolysis. The values of the activation energy calculated for both mechanisms were 67.17 and 58.03 kJ mol(-1), respectively.
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页数:13
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