Abstract
Biodiesel is a free fatty acid methyl ester (FAME) produced from transesterification of oil and short-chain alcohol. Nowadays, the cost of conventional biodiesel production might not be competitive with petro-diesel due to the cost of refined oil as a main feedstock. Many challenging researches have proposed method or technology to efficiently produce biodiesel. One of the most important knowledge is the synthesis of the suitable catalyst for biodiesel production. Solid acid catalyst is a promising catalyst to produce biodiesel from low-cost feedstocks since it can catalyze simultaneously esterification of free fatty acid (FFA) and transesterification of triglyceride. To improve the biodiesel CO2 cycle, the waste material, coffee residue, was selected as a supported catalyst. It provides the appropriate textural properties such as high surface area with mesoporous structure and hydrophobic properties. The sulfonation with concentrated H2SO4 was used for additional acidic functional group which exhibits a strong protonic acid site density. Therefore, this research aims to synthesize sulfonated activated carbon derived from coffee residue (SCAC) to catalyze esterification of caprylic acid as a model of FFA. The sulfonation temperature varied from 140 to 200 °C as named SCAC-140, SCAC-160, SCAC-180, and SCAC-200 catalysts.
After sulfonation process, the X-ray diffraction (XRD) patterns of all catalysts were similar to coffee residue activated carbon (CAC) as a support. A few, broad peak at 2θ = 15–30° and 30–50°, were related to amorphous carbon and graphene sheet at the plane C (101), respectively. Fourier transform infrared spectroscopy (FT-IR) of CAC at 3400 cm− 1 was absent which confirmed the hydrophobic property of this support. FT-IR spectra of SCAC catalysts illustrated the acid function as 3400, 1700, 1600, 1300, 1000, and 1100 cm− 1 , which is related to O–H stretching mode of COOH and phenolic, C═O of COOH, C═C of polyaromatic, O═S═O symmetric SO2 stretching, O═S═O asymmetric SO2 stretching, respectively. SCAC-180 catalyst exhibited the highest initial rate due to the highest total acid site density which included sulfonated, carboxylic, and phenolic group. At 2 h, SCAC-200 showed the highest caprylic acid conversion while SCAC-140 provided the lowest caprylic acid conversion. It was probably due to the textural and structural properties of these synthesized catalysts. All of synthesized carbon catalysts demonstrated the higher catalytic activity than that of Amberlyst-15. However, the solid acid catalyst still provided a lower catalytic activity as compared to homogeneous H2SO4 catalyst.
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References
Coronado CR, de Carvalho JA, Silveira JL (2009) Biodiesel CO2 emissions: a comparison with the main fuels in the Brazilian market. Fuel Process Technol 90:204–211
Wu X, Leung DYC (2011) Optimization of biodiesel production from camelina oil using orthogonal experiment. Appl Energy 88:3615–3624
Sani YM, Daud WMAW, Aziz ARA (2014) Activity of solid acid catalysts for biodiesel production: a critical review. Appl Catal a-Gen 470:140–161
Silva VWD, Laier LO, da Silva MJ (2010) Novel H3PW12O40: catalysed esterification reactions of fatty acids at room temperature for biodiesel production. Catal Lett 135:207–211
Baig A, Ng FTT (2010) A single-step solid acid-catalyzed process for the production of biodiesel from high free fatty acid feedstocks. Energy Fuel 24:4712–4720
Suwannakarn K, Lotero E, Ngaosuwan K, Goodwin JG (2009) Simultaneous free fatty acid esterification and triglyceride transesterification using a solid acid catalyst with in situ removal of water and unreacted methanol. Ind Eng Chem Res 48:2810–2818
Ngaosuwan K, Mo XH, Goodwin JG, Praserthdam P (2010) Reaction kinetics and mechanisms for hydrolysis and transesterification of triglycerides on tungstated zirconia. Top Catal 53:783–794
Chen SY, Mochizuki T, Abe Y, Toba M, Yoshimura Y (2014) Ti-incorporated SBA-15 mesoporous silica as an efficient and robust Lewis solid acid catalyst for the production of high-quality biodiesel fuels. Appl Catal B-Environ 148:344–356
Jitputti J, Kitiyanan B, Rangsunvigit P, Bunyakiat K, Attanatho L, Jenvanitpanjakul P (2006) Transesterification of crude palm kernel oil and crude coconut oil by different solid catalysts. Chem Eng J 116:61–66
Li Y, Zhang XD, Sun L, Xu M, Zhou WG, Liang XH (2010) Solid superacid catalyzed fatty acid methyl esters production from acid oil. Appl Energy 87:2369–2373
Lam MK, Lee KT, Mohamed AR (2009) Sulfated tin oxide as solid superacid catalyst for transesterification of waste cooking oil: an optimization study. Appl Catal B-Environ 93:134–139
Konwar LJ, Boro J, Deka D (2014) Review on latest developments in biodiesel production using carbon-based catalysts. Renew Sust Energy Rev 29:546–564
Boonamnuayvitaya V, Chaiya C, Tanthapanichakoon W (2004) The preparation and characterization of activated carbon from coffee residue. J Chem Eng Jpn 37:1504–1512
Toda M, Takagaki A, Okamura M, Kondo JN, Hayashi S, Domen K, Hara M (2005) Green chemistry—biodiesel made with sugar catalyst. Nature 438:178–178
Kastner JR, Miller J, Geller DP, Locklin J, Keith LH, Johnson T (2012) Catalytic esterification of fatty acids using solid acid catalysts generated from biochar and activated carbon. Catal Today 190:122–132
Shu Q, Zhang Q, Xu GH, Nawaz Z, Wang DZ, Wang JF (2009) Synthesis of biodiesel from cottonseed oil and methanol using a carbon-based solid acid catalyst. Fuel Process Technol 90:1002–1008
Lou WY, Guo Q, Chen WJ, Zong MH, Wu H, Smith TJ (2012) A highly active bagasse-derived solid acid catalyst with properties suitable for production of biodiesel. Chemsuschem 5:1533–1541
Liu F, Sun J, Sun Q, Zhu L, Wang L, Meng X, Qi C, Xiao F-S (2012) High-temperature synthesis of magnetically active and SO3H-functionalized ordered mesoporous carbon with good catalytic performance. Catal Today 186:115–120
Mar WW, Somsook E (2012) Sulfonic-functionalized carbon catalyst for esterification of high free fatty acid. Procedia Eng 32:212–218
Kitano M, Arai K, Kodama A, Kousaka T, Nakajima K, Hayashi S, Hara M (2009) Preparation of a sulfonated porous carbon catalyst with high specific surface area. Catal Lett 131:242–249
Fu P, Hu S, Xiang J, Sun L, Su S, Wang J (2012) Evaluation of the porous structure development of chars from pyrolysis of rice straw: effects of pyrolysis temperature and heating rate. J Anal Appl Pyrolysis 98:177–183
Okamura M, Takagaki A, Toda M, Kondo JN, Domen K, Tatsumi T, Hara M, Hayashi S (2006) Acid-catalyzed reactions on flexible polycyclic aromatic carbon in amorphous carbon. Chem Mater 18:3039–3045
Zong MH, Duan ZQ, Lou WY, Smith TJ, Wu H (2007) Preparation of a sugar catalyst and its use for highly efficient production of biodiesel. Green Chem 9:434–437
Acknowledgements
The author would like to thank Thailand Research Fund (TRF) and Rajamangala University of Technology Krungthep, and the Commission on Higher Education for supporting by grant fund under the MRG program with ID of MRG5080040. The author also would like to thank the Center of Excellence on Catalysis and Catalytic Reaction Engineering and Moccona company (Thailand) for providing analysis facility and coffee residue, respectively.
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Ngaosuwan, K. (2015). Solid Acid Catalyst Derived from Coffee Residue for Biodiesel Production. In: Sayigh, A. (eds) Renewable Energy in the Service of Mankind Vol I. Springer, Cham. https://doi.org/10.1007/978-3-319-17777-9_5
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DOI: https://doi.org/10.1007/978-3-319-17777-9_5
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