|
|
|
|
LEADER |
02117 am a22002413u 4500 |
001 |
93691 |
042 |
|
|
|a dc
|
100 |
1 |
0 |
|a Abdul Mutalib, Aunie Afifah
|e author
|
700 |
1 |
0 |
|a Ibrahim, Mohd. Lokman
|e author
|
700 |
1 |
0 |
|a Matmin, Juan
|e author
|
700 |
1 |
0 |
|a Kassim, Muhd. Firdaus
|e author
|
700 |
1 |
0 |
|a Mastuli, Mohd. Sufri
|e author
|
700 |
1 |
0 |
|a Yap, Yun Hin Taufiq
|e author
|
700 |
1 |
0 |
|a Mohd. Shohaimi, Norshahidatul Akmar
|e author
|
700 |
1 |
0 |
|a Islam, Aminul
|e author
|
700 |
1 |
0 |
|a Tan, Yie Hua
|e author
|
700 |
1 |
0 |
|a Mohd. Kaus, Noor Haida
|e author
|
245 |
0 |
0 |
|a SiO2-rich sugar cane bagasse ash catalyst for transesterification of palm oil
|
260 |
|
|
|b Springer,
|c 2020.
|
856 |
|
|
|z Get fulltext
|u http://eprints.utm.my/id/eprint/93691/1/JuanMatmin2020_SiO2RichSugarCaneBagasseAshCatalyst.pdf
|
520 |
|
|
|a This study demonstrated the performance of the sugarcane bagasse ash (SCBA) impregnated with calcium oxide (CaO) as a novel heterogeneous basic catalyst in biodiesel production. The SCBA was prepared by calcination for 2 h at 500 to 800 °C and impregnated with CaO loadings (10 to 40 wt.%). The prepared SCBA/CaO catalyst was characterized using Fourier transform infrared spectroscopy (FTIR), scanning electron microscopy (SEM), X-ray diffraction (XRD), temperature programmed desorption of carbon dioxide (TPD-CO2), thermal gravimetric analysis (TGA), X-ray fluorescence (XRF) and Brunauer-Emmett-Teller (BET) surface characteristics. A series of transesterification reactions were conducted to evaluate the performance of the catalysts. As a result, highest FAME yield of 93.8% was obtained by using SCBA600°C CaO(40%) catalyst at 20:1 methanol-to-oil molar ratio, reaction temperature of 65 °C, with 6 wt.% catalyst in 3 h. Besides, the catalyst can be reused up to 5 reaction cycles with biodiesel yield of 93.0% and 70.3% at first and fifth cycles, respectively. In this work, it was found that the natural SiO2 in the SCBA has a significant role to enhance the catalytic performance and reduce the catalyst's deactivation drawback by minimizing the leaching of active sites.
|
546 |
|
|
|a en
|
650 |
0 |
4 |
|a QD Chemistry
|