* Corresponding Author
PREPARATION, CHARACTERIZATION AND CATALYTIC ACTIVITY TEST OF CoMo/ZnO CATALYST ON ETHANOL CONVERSION USING STEAM REFORMING METHOD
https://doi.org/10.22146/ijc.21529 Wega Trisunaryanti(1*), Handirofa Handirofa(2), Triyono Triyono(3), Suryo Purwono(4)
(1) Department of Chemistry, Faculty of Mathematics and Natural Sciences Gadjah Mada University, Sekip Utara Yogyakarta 55281
(2) Department of Chemistry, Faculty of Mathematics and Natural Sciences, Gadjah Mada University, Sekip Utara, Yogyakarta 55281, Indonesia
(3) Department of Chemistry, Faculty of Mathematics and Natural Sciences, Gadjah Mada University, Sekip Utara, Yogyakarta 55281, Indonesia
(4) Department of Chemical Engineering, Faculty of Engineering, Gadjah Mada University, Jl. Grafika, Yogyakarta 55281
(*) Corresponding Author
Abstract
Preparation, characterization and catalytic activity test of CoMo/ZnO catalyst for steam reforming of ethanol have been investigated. The catalysts preparation was carried out by impregnation of Co and/or Mo onto ZnO sample. Water excess was used in ethanol feed for steam reforming process under mol ratio of ethanol:water (1:10). Characterizations of catalysts were conducted by analysis of metal content using Atomic Absorption Spectroscopy (AAS). Determination of catalysts acidity was conducted by gravimetric method of adsorption of pyridine base. Catalytic activity test on ethanol conversion using steam reforming method was conducted in a semi-flow reactor system, at a temperature of 400 oC, for 1.5 h under N2 flow rate of 10 mL/min. Gas product was analyzed by gas chromatograph with TCD system. The results of catalysts characterizations showed that the impregnation of Co and/or Mo metals on ZnO sample increased its acidity and specific surface area. The content of Co in Co/ZnO and CoMo/ZnO catalysts was 1.14 and 0.49 wt%. The Mo content in CoMo/ZnO catalyst was 0.36 wt%. The catalytic activity test result on ethanol conversion showed that the ZnO, Co/ZnO, and CoMo/ZnO catalysts produced gas fraction of 16.73, 28.53, and 35.53 wt%, respectively. The coke production of ZnO, Co/ZnO, and CoMo/ZnO catalysts was 0.86, 0.24, and 0.08 wt%, respectively. The gas products consisted mainly of hydrogen.
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[1] Fatsikostas, A.N., Kondarides, D.I., and Verykios, X.E., 2001, Chem. Commun., 851-852.
[2] Al-Qahtani, H., 1997, J. Chem. Eng., 66,51-56.
[3] Augustine, R.L., 1996, Heterogenous catalysis for the Synthetic Chemist, Marcel Dekker Inc., New York.
[4] Aupretre, F., Descorme, C., and Duprez, D., 2002, Catal. Commun., 3, 263-267.
[5] Batista, M.S., Santos, R.K.S., Assaf, E.M., Assaf, J.M., and Ticianelli, E.A., 2004, J. Power Sources, 134, 27-32.
[6] Bridgewater, A.J., Burch, R., and Mitchell, P.C.H., 1980, J. Chem. Soc., Faraday Trans. 1, 76, 1811-1820.
[7] Galvita, V.V., Belyaev, V.D., Semikolenov, V.A., Tsiakaras, P., Frumin, A., and Sobyanin, V.A., 2002, React. Kinet. Catal. Lett., 343-351.
[8] Haga, F., Nakajima, T., Miya, H., and Mishima, S., 1997, Catal. Lett., 48, 223-227.
[9] Llorca, J., Homs, N., Sales, J., and de la Piscina, P.R., 2002, J. Catal., 209, 306-317.
[10] Llorca, J., Homs, N., Sales, J., Fierro,l J.L.G., and de la Piscina, P.R., 2004, J. Catal., 222, 470-480.
[11] Resini, C., Delgado, M.C.H., Arrighi, L., Alemany, L.J., Marazza, R., and Busca, G., 2005, Catal. Commun., 6, 441-445.
[12] Trimm, D.L., 2005, Appl. Catal., A, 296, 1-11.
DOI: https://doi.org/10.22146/ijc.21529
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Indonesian Journal of Chemistry (ISSN 1411-9420 /e-ISSN 2460-1578) - Chemistry Department, Universitas Gadjah Mada, Indonesia.