Synthesis of novel graphene oxide/bentonite bi-functional heterogeneous catalyst for one-pot esterification and transesterification reactions. (1st September 2018)

• Record Type: Journal Article
• Authors: Ali, Basit; Yusup, Suzana; Quitain, Armando T.; Alnarabiji, Mohamad Sahban; Kamil, Ruzaimah Nik M.; Kida, Tetsuya
• Is Part Of: Energy conversion and management. Volume 171(2018)
• Page Start: 1801
• Page End: 1812
• Publication Date: 2018-09-01
• Subjects: GO-NaOH-bentonite -- Impregnation -- Esterification -- Transesterification -- Biodiesel; Direct energy conversion -- Periodicals; Energy storage -- Periodicals; Energy transfer -- Periodicals; Énergie -- Conversion directe -- Périodiques; Direct energy conversion; Periodicals; 621.3105
• DOI: 10.1016/j.enconman.2018.06.082
• Languages: English
• ISSNs: 0196-8904

Abstract

Graphical abstract: Highlights: GO-NaOH-bentonite was synthesized as a novel heterogeneous composite catalyst. The catalyst performed simultaneous esterification and tranesterification. The high Brønsted Acidic sites of GO played the key role in esterification of FFA. GO-NaOH-bentonite improved the accessibility of methanol to oil and FFA. Abstract: Several heterogeneous catalysts have been utilized for biodiesel synthesis from low-grade oils containing free fatty acids (FFA) in a two-stage esterification and transesterification method in previous studies. In this study, NaOH-bentonite impregnated with graphene oxide (GO), as a novel bi-functional heterogeneous catalyst for simultaneous esterification and transesterification was developed and characterized by thermogravimetric analysis (TGA), X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), Raman spectroscopy, field emission scanning electron microscopy (FESEM), N2 adsorption measurement to obtain the surface area (BET) and temperature programmed desorption (TPD NH3 and CO2 ). The effect of reaction time (h), reaction temperature (°C), methanol-to-oil ratio and catalyst amount (wt%) was studied. All experiments were performed at an optimized GO-to-NaOH-bentonite ratio of 1:20. Impressively, the GO-NaOH-bentonite catalyst exhibited excellent catalytic performance and resulted in 89.5 wt% conversion of free fatty acids and 98.5 wt% overall biodiesel yield after 4.5 h reaction time with catalyst amount of 6 wt%, reaction temperature of 62 °C and 6:1 methanol-to-oil ratio. Results showed that the presence of Na2 O enhanced the low-strength basic sites of the catalyst at 150–200 °C, which played the key role in transesterification of rapeseed oil. It was also found that, the presence of GO on NaOH-bentonite, increased the overall acid strength of the composite catalyst by providing more Brønsted acidic sites. The acidic-basic nature of GO-NaOH-bentonite improved the accessibility of methanol to oil and FFA with the increased pore size of the composite catalyst.