Abstract
Biofuel additive catalytic activity was tested by supported heteropoly acid at different composition on bentonite, mobil composition of matter no. 41 (MCM-41) materials. It has been found that catalyst activity is affected by each dodecatungsto-phosphoric acid (DTP) concentration and types of support. Maximum selectivity towards di- and triacetin was observed with increasing concentration of DTP from 10 to 60% with MCM-41 and BNT support. Prepared catalyst with 60% DTP/BNT was showed maximum selectivity towards di- and triacetin about 94%. The catalysts were characterized by XRD, FT-IR, and TGA/DTA analysis. The various trials on 1% and 2% mixture of the major product (di- + triacetin) additive obtained from esterification of glycerol biomass with acetic acid via 60% DTP/BNT catalyst to check characteristics of biofuels additive. The product has 2% (di- + triacetin) blend showed excellent performance as compared with conventional diesel biofuel additives.
Graphical abstract
Similar content being viewed by others
Data availability
No data availability and all data are provided in full in the results section of this paper.
References
Alves AC, Neto ADBS, Besa BDS, Oliveira AC, Filho JM, Campos AF, Oliveira AC (2016) Binary oxides with defined hierarchy of pores in the esterification of glycerol. Cataly 6:1–24. https://doi.org/10.3390/catal6100151
Carvalho DCD, Oliveira AC, Ferreira OP, Filho JM, Tehuacanero-Cuapa S, Oliveira AC (2017) Titanate nanotubes as acid catalysts for acetalization of glycerol with acetone: influence of the synthesis time and the role of structure on the catalytic performance. Chem.Engg.j 1–48:1454–1467. https://doi.org/10.1016/j.cej.2016.11.047
Wang X, Shang C, Wu G, Liu X, Liu H (2016) Base-free selective oxidation of glycerol over LDH hosted transition metal complexes using 3 % H2O2 as oxidant. Catal 6:1–10. https://doi.org/10.3390/catal6070101
Ummadisetti C, Rachapudi BN, LA Praasd B, Prabhavathi D (2014) Glycerol valorization as biofuel additives by employing a carbon-based solid acid catalyst derived from glycerol. Ind Eng Chem Res 53:16164–16169. https://doi.org/10.1021/ie503079m
Zhu S, Gao X, Dong F, Zhu Y, Zheng H, Li Y (2013) Design of a highly active silver-exchanged phosphotungstic acid catalyst for glycerol esterification with acetic acid. J Catal 306:155–163. https://doi.org/10.1016/j.jcat.2013.06.026
Magar S, Mohanraj GT, Jana SK, Rode CV (2020) Synthesis and characterization of supported heteropoly acid: efficient solid acid catalyst for glycerol esterification to produce biofuel additives. Inorg Nano metal Chem 50:1157–1165. https://doi.org/10.1080/24701556.2020.1737817
Mufrodi Z (2012) Chemical kinetics for synthesis of triacetin from biodiesel by-product.Inter.J. Chem 4:101–107. https://doi.org/10.5539/ijc.v4n2p101
Nanda MR, Zhang Y, Yuan Z, Qin W, Ghaziaskar HS, Xu C (2016) Catalytic conversion of glycerol for sustainable production of solketal as a fuel additive: a review Renew. Sustain Energy Rev 56:1022–1031. https://doi.org/10.1016/j.rser.2015.12.008
Tangestanifard M, Ghaziaskar HS (2017) Arenesulfonic acid-functionalized bentonite as catalyst in glycerol esterification with acetic acid. Catal 7:1–11. https://doi.org/10.3390/catal7070211
Caballero KV, Guerrero-Amaya H, Baldovino-Medrano VG (2019) Revisiting glycerol esterification with acetic acid over Amberlyst-35 via statistically designed experiments: overcoming transport limitations. Chem Eng Sci 207:91–104. https://doi.org/10.1016/j.ces.2019.06.003
Garade AC, Kshirsagar VS, Jha A, Rode CV (2010) Structure-activity studies of dodecatungstophosporic acid impregnated bentonite clay catalyst in hydroalkylation of p-cresol. Catal Commun 11:942–945. https://doi.org/10.1016/j.catcom.2010.04.008
Magar S, Kamble S, Mohanraj GT, Jana SK, Rode CV (2017) Solid-acid-catalyzed etherification of glycerol to potential fuel additives. Energy Fuels 31(11):12272–12277. https://doi.org/10.1021/acs.energyfuels.7b02213
Sakate SS, Kamble SB, Chikate RC, Rode CV (2017) MCM-41-supported phosphotungstic acid-catalyzed cleavage of C-O bond in allyl aryl ethers. New J Chem 41:4943–4949. https://doi.org/10.1039/C7NJ00375G
Xiao L, Mao J, Zhou J, Guo X, Zhang S (2011) Enhanced performance of HY zeolites by acid wash for glycerol etherification with isobutene. Appl Catal A Gen 393:88–95. https://doi.org/10.1016/2Fj.apcata.2010.11.029
Rode CV, Garade AC, Chikate RC (2009) Solid acid catalyst: modification of acid sites and effect on activity and selectivity tuning in various reactions. Catal Surv Asia 13:205–220. https://doi.org/10.1007/s10563-009-9078-4
Subhash, M., Pal, D. B., Jana, SK (2021) Biofuels additives derived via clay supported heteropoly acid catalyzed etherification of glycerol with t-butanol-biomass to liquid oxygenates. Chem Pap 1–10.
Kamble SB, More S, Rode CV (2016) Highly selective direct azidation of alcohols over a heterogeneous povidone–phosphotungstic solid acid catalyst. New J Chem 40:10240–10245. https://doi.org/10.1039/C6NJ02500E
Izumi Y, Ogawa M, Urabe K (1995) Alkali metal salts and ammonium salts of Keggin-type heteropoly acids as solid acid catalyst for liquid – phase Friedel-Crafts reactions. Appl Catal A 132:127–140. https://doi.org/10.1016/0926-860X(95)00167-0
Resitoglu IA, Altinisik K, Keskin A (2015) The pollutant emissions from diesel-engine vehicles and exhaust after treatment systems, clean technologies and environmental policy 17:15–27. https://doi.org/10.1007/s10098-014-0793-9
Mukhopadhyay P, Chakraborty R (2015) Effects of bio glycerol-based fuel additives on diesel fuel property, engine performance and emission quality: a review. Energy Procedia 71:671–676. https://doi.org/10.1016/j.egypro.2015.11.553
Fernando S, Hall C, Jha S (2006) NOx Reduction from biodiesel fuels. Energy Fuels 20:376–382. https://doi.org/10.1021/ef050202m
Rao PV, Appa Rao BV (2012) Performance and emission characteristics of diesel engine with COME-triacetin additive blends as fuel. Int J Energy Environ 3:629–638
Goncalves VLC, Pinto BP, Silva JC, Mota CJA (2008) Acetylation of glycerol catalyzed by different solid acids. Catal Today 133–135:673–677. https://doi.org/10.1016/j.cattod.2007.12.037
Zhou L, Al-Zaini E, Adesina AA (2013) Catalytic characterization and parameters optimization of the glycerol acetylation over solid acid catalysts. Fuel 103:617–625. https://doi.org/10.1016/j.fuel.2012.05.042
Khayoon M-S, Triwahyono S, Hameed B-H, Jalil A-A (2014) Improved production of fuel oxygenates via glycerol acetylation with acetic acid. Chem Eng J 243:473–484. https://doi.org/10.1016/j.cej.2014.01.027
Rane SA, Pudi SM, Biswa P (2016) Esterification of glycerol with acetic acid over active and stable alumina-based catalysts: a reaction kinetics study. Chem Biochem Eng 30(1):33–45. https://doi.org/10.15255/CABEQ.2014.2093
Keogh J, Tiwari MS, Manyar H (2019) Esterification of glycerol with acetic acid using nitrogen-based Bronsted-acidic ionic liquids. Ind Eng Chem Res 58(37):17235–17243. https://doi.org/10.1021/acs.iecr.9b01223
Barrault J, Pouilloux Y, Clacens JM, Bancquart VS (2002) Catalysis and fine chemistry. Catal Today 75:177–181. https://doi.org/10.1016/S0920-5861(02)00062-7
Ekinci EK (2019) Oktar N (2019) Production of value-added chemicals from esterification of waste glycerol over MCM-41 supported catalysts. Green Process Synth 8:128–134. https://doi.org/10.1515/gps-2018-0034
Huang R, Kim Y (2015) Catalytic synthesis of glycerol tert-butyl ethers as fuel additives from the biodiesel by-product glycerol. J Chem 2015:1–6. https://doi.org/10.1155/2015/763854
Kotwal M, Deshpande DS (2011) Esterification of fatty acids with glycerol over Fe–Zn double-metal cyanide catalyst. Catal Commu 12:1302–1306. https://doi.org/10.1016/j.catcom.2011.05.008
Lei Q, Li D, Li J-F, Liu C-L, Xu C, Dong W-S (1019) glycerol esterification to glyceryl diacetate over SO42-/W-Zr complex solid super acid catalysts. Chemistry Select 4(9):2780–2786. https://doi.org/10.1002/slct.201803820
Manriquez-Ramirez ME, Elizalde I, Ramirez-López R, Trejo-Valdez M, Estrada-lores M (2020) Acetylation of glycerol using MgO–CaO catalystswith different CaO loadings reaction kinetics, mechanisms and catalysis, 130: 417–431. https://doi.org/10.1007/s11144-020-01774-z
Acknowledgements
The authors are thankful to BIT the Mesra Central equipment facility for characterization for finalizing the manuscript.
Author information
Authors and Affiliations
Contributions
MS has done the all experiments and writes manuscript, and SKJ and DBP edit and review the manuscript.
Corresponding authors
Ethics declarations
Ethics approval
There is no involvement of human or animal cell in this work.
Conflict of interest
The authors declare no competing interests.
Additional information
Publisher's note
Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.
Statement of novelty
Commercialization of biodiesel manufacture is well practiced in last couple of decades as it offers Sustainability and minimization of emission of greenhouse gasses compared to the fossil-based fuels. Coproduction of 10% crude glycerol is associated with bio-diesel production and the significant amount of bio-glycerol remaining unutilized poses one of the challenges to bio-diesel industry. Several options of glycerol biomass valorization have been proposed with some of them having commercial potential. Glycerol etherification is one such attractive process in the production of an excellent fuel additive that has great potential in the reformation of diesel. The research program has been undertaken for investigation of transesterification of bio-derived with acetic acid to form the major di- and triacetins which are less viscous and high volatile biofuel additives. Commonly, the use of bio-origin fuel additives enhances the thermal efficiency of diesel engine with less pollutants emission and increases other fuel properties such as cloud and pour point.
Rights and permissions
About this article
Cite this article
Magar, S.B., Pal, D.B. & Jana, S.K. Synthesis of different heteropoly acid catalysts for transesterification of bio-derived glycerol to produce oxygenated fuel additive for energy utilization. Biomass Conv. Bioref. 14, 6939–6949 (2024). https://doi.org/10.1007/s13399-022-02838-x
Received:
Revised:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s13399-022-02838-x