Abstract
The present work encompasses the production of biodiesel from an inexpensive waste, viz., used rice bran oil (URBO) through concurrent esterification and transesterification reactions employing the prepared waste duck bone (WDB)-derived natural hydroxyapatite (NAHAp) supported vanadium impregnated solid catalyst (VNAHAp). The optimal VNAHAp catalyst possessed 92.23 m2/g surface area which was much superior to 61.46 m2/g of the V-catalyst (VCHAp) prepared using commercially available hydroxyapatite (CHAp). The optimal (Box–Behnken design) concurrent trans/esterification reaction conditions for biodiesel (FAME) production from URBO and methanol were 5 wt.% catalyst concentration, 8:1 methanol/URBO mole ratio, and 35 wt% NH4VO3 loaded VNAHAp (35VNAHAp) catalyst that resulted in 99.05% FAME yield deploying a low-energy infrared radiator assisted batch reactor (LIRABR) which ensured significantly high FAME yield at milder temperature (60°C) and in shorter reaction time (30 min) compared to a conventionally heated batch reactor. The product biodiesel and its blend with commercial diesel conformed to ASTM D7467-10 specifications. The life cycle assessment (LCA) of the entire process advocated superior sustainability of the biodiesel production using 35VNAHAp catalyst in the LIRABR compared to their conventional counterparts. Valorization of two potential wastes, viz., URBO and WDB, under milder process conditions involving LIRABR and 35VNAHAp resulted in lower environmental impacts, thus rendering a sustainable biodiesel production process towards a greener earth.
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Data availability
The datasets generated during and/or analyzed during the current study are available from the corresponding author on reasonable request.
Abbreviations
- URBO:
-
used rice bran oil
- WDB:
-
waste duck bone
- NAHAp:
-
natural hydroxyapatite
- VNAHAp:
-
vanadium impregnated solid catalyst
- CHAp:
-
commercially available hydroxyapatite
- FAME:
-
biodiesel
- LIRABR:
-
low-energy infrared radiator assisted batch reactor
- CSBR:
-
conventional stirred batch reactor
- LCA:
-
life cycle assessment
- LCI:
-
life cycle inventory
- FAETP:
-
fresh water aquatic eco toxicity potential
- MAETP:
-
marine aquatic eco toxicity potential
- HTP:
-
human toxicity potential
- GWP:
-
global warming potential
- R PL :
-
precursor loading
- R CC :
-
catalyst concentration
- R MR :
-
methanol/URBO molar ratio
- ψ FAME :
-
FAME yield (%)
- P FAME :
-
produced biodiesel
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Acknowledgements
The authors acknowledge the support provided by the WEES 2020 International conference, NIT Durgapur, India.
Funding
The financial supports of the Department of Science & Technology and Biotechnology; Government of West Bengal (File No. ST/P/S&T/4G-2/2018); RUSA 2.0 (Ref. No. R-11/481/19 and Ref. No. R-11/316/19) Jadavpur University, India; and Council of Scientific and Industrial Research (Grant/Award Number: 09/096/(0975)/2019/EMR/I) are gratefully acknowledged.
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PP conducted the experiments, analyzed and interpreted the data, and prepared the draft manuscript under the guidance of RC. PK analyzed and interpreted the data, software, and wrote the draft manuscript with the support of RC. Besides, RC designed and developed the reactor, conceptualized and supervised the entire research, and wrote and edited the final manuscript. All authors read and approved the final manuscript.
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Pradhan, P., Karan, P. & Chakraborty, R. Life cycle sustainability assessment of optimized biodiesel production from used rice bran oil employing waste derived-hydroxyapatite supported vanadium catalyst. Environ Sci Pollut Res 29, 20064–20077 (2022). https://doi.org/10.1007/s11356-021-16482-x
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DOI: https://doi.org/10.1007/s11356-021-16482-x