2021
DOI: 10.1016/j.catcom.2020.106201
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Efficient reaction for biodiesel manufacturing using bi-functional oxide catalyst

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Cited by 47 publications
(24 citation statements)
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“…As depicted in Fig. 1, the XRD patterns of CaO peaks appeared at 2-theta value of 37.34°, 53.82°, 64.11° and 67.35° (JCPDS pattern 01-082-1691) [25][26][27][28].…”
Section: Results and Discussion 31 Catalysts Characterizationmentioning
confidence: 93%
See 1 more Smart Citation
“…As depicted in Fig. 1, the XRD patterns of CaO peaks appeared at 2-theta value of 37.34°, 53.82°, 64.11° and 67.35° (JCPDS pattern 01-082-1691) [25][26][27][28].…”
Section: Results and Discussion 31 Catalysts Characterizationmentioning
confidence: 93%
“…1. The XRD pattern of ZnO exhibited at 2-theta 31.73°, 34.41°, 36.23°, 47.53°, 56.53°, 62.81°, 66.32°, 67.90°, 69.02°, 72.53° and 76.90°, which corresponds to hexagonal zincite structure (JCPDS pattern 01-075-7917) [25,26]. As depicted in Fig.…”
Section: Results and Discussion 31 Catalysts Characterizationmentioning
confidence: 93%
“…2D Na/ITQ-2 is a two-dimensional basic zeolite contains natrium and ITQ-2 zeolite which possess large external surface areas, hierarchical characteristics, stable active sites, and a high concentration of strong basic sites that contribute to enhancing the mass transfer of bulky molecules and providing more accessible and stable active sites in the transesterification of bio-derived oil to produce biodiesel. A similar investigation conducted by Mansir et al [101] using bimetallic tungsten zirconia (W-Zr) samples to catalyze simultaneous esterification and transesterification of unrefined palm-derived waste oil (PDWO) to biodiesel. The catalyst with a 7 wt% concentration of W-Zr loaded on CaO support (7WZC) was able to achieve a maximum biodiesel yield of 94% in one-hour reaction time under the optimum reaction condition (methanol and oil molar ratio of 15:1, 2 wt% catalyst loading, 80 • C reaction temperature).…”
Section: Transesterificationmentioning
confidence: 98%
“…As could be seen, the conversion of oleic acid decreased after each run from 45.7% (first run) to 17.9% (sixth run) for the HPW@CoCe-MOF catalyst, and the possible reasons for the reduction substantially of conversion are the blockage of the CoCe-MOF channel. On the contrary, the conversion of oleic acid decreased slightly after each run from 67.2% (first run) to 61.8% (eighth run) for the HPW@CoCeO catalyst, and the decrease in catalytic activity could be related to the adsorption of oleic acid, methanol, or water molecule on the active sites of the HPW@CoCeO composite during each run [39]. e collected catalyst from the eighth reaction cycle was characterized by FTIR (Figure 2).…”
Section: Recyclability and Leaching Test Of The Hpw@coceomentioning
confidence: 99%