* Corresponding Author
CATALYTIC HYDROCRACKING OF WASTE LUBRICANT OIL INTO LIQUID FUEL FRACTION USING ZnO, Nb2O5, ACTIVATED NATURAL ZEOLITE AND THEIR MODIFICATION
https://doi.org/10.22146/ijc.21589 Wega Trisunaryanti(1*), Suryo Purwono(2), Arista Putranto(3)
(1) Department of Chemistry, Faculty of Mathematics and Natural Sciences, Universitas Gadjah Mada, Sekip Utara, Yogyakarta 55281
(2) Department of Chemical Engineering, Faculty of Engineering, Universitas Gadjah Mada, Jl. Grafika, Yogyakarta 55281
(3) Department of Chemistry, Faculty of Mathematics and Natural Sciences, Universitas Gadjah Mada, Sekip Utara, Yogyakarta 55281
(*) Corresponding Author
Abstract
Catalytic hydrocracking of waste lubricant oil into liquid fuel fraction using ZnO, Nb2O5, activated natural zeolite (ZAAH) and their modification has been investigated. The zeolite was produced in Wonosari, Yogyakarta. Activation of the zeolite was carried out by refluxing with HCl 3M for 30 min, produced the activated natural zeolite (ZAAH). The ZnO/ZAAH catalyst was prepared by impregnation of Zn onto the ZAAH by ion exchange method using salt precursor of Zn(NO3)2.4H2O. The Nb2O5/ZAAH catalyst was prepared by mixing the ZAAH sample with Nb2O5 and oxalic acid solution until the paste was formed. The impregnation of Zn onto Nb2O5/ZAAH was carried out using the same method to that of the ZnO/ZAAH catalyst resulted ZnO/Nb2O5-ZAAH catalyst. Characterization of catalyst includes determination of Zn metal by Atomic Absorption Spectroscopy (AAS), acidity by gravimetric method and catalyst porosity by Surface Area Analyzer (NOVA-1000). Catalytic hydrocracking was carried out in a semi-batch reactor system using ZnO, ZAAH, ZnO/ZAAH and ZnO/Nb2O5-ZAAH catalysts at 450 oC under the H2 flow rate of 15 mL/min. and the ratio of catalyst/feed = 1/5. The composition of liquid products was analyzed by Gas Chromatograpy (GC).The results showed that impregnation of ZnO and/or Nb2O5 on the ZAAH increased the acidity and specific surface area of catalyst. The products of the hydrocracking process were liquid, coke and gas. Conversion of liquid products was increased by the increase of catalyst acidity. The highest liquid product was produced by ZnO/Nb2O5-ZAAH catalyst, 52.97 wt-%, consist of gasoline, 38.87 wt-% and diesel, 14.10 wt-%.
Keywords
Full Text:
Full Text PdfReferences
[1] Sasaoka, E., Iwamoto, Y., Hirano, S., Uddin, M.A., and Sakata, Y., 2001, Energy Fuels, 9, 344.
[2] White, J.D., Groves, Jr.F.R., and Harrison, D.P., Catal. Today, 2000, 40, 47.
[3] Bhaskar, T., Uddin, M. A., Muto, A., Sakata, Y., Omura, Y., Kimura, K., and Kawakami, Y., 2004, J. Fuel., 83, 9-15.
[4] Trisunaryanti, W., Shiba, R., Miura, M., Nomura, M., Nishiyama, N., and Matsukata, M., 1996, J. Jpn. Inst. Petr., 39, 1, 20-25.
[5] Sawa, M., Niwa, M., and Murakami, W., 2000, Zeolites, 10, 532-538.
[6] Trisunaryanti, W. and Khairinal, 2000, Dealuminasi zeolit alam Indonesia dengan perlakuan asam dan hidrotermal, Prosiding Seminar Nasional Kimia VII FMIPA-UGM, Yogyakarta.
[7] Trisunaryanti, W. and Purwono, S., 2007, Pengaruh Perlakuan HCl dan Na2EDTA Terhadap Karakter Zeolit Alam dan Impregnasi ZnO, Nb2O5 Terhadap Keasaman Katalis, Seminar Kemajuan Terkini Penelitian Klaster Sains-Teknologi Universitas Gadjah Mada, Yogyakarta.
[8] Chareonpanich, M., Zhang, Z., and Tomita, A., 1996, Energy Fuels, 10, 927-931.
[9] Weissman, J.G., 2000, Catal. Today, 28, 159-166.
[10] Geantet, C., Afonso, J., Breysce, M., Alali, N., and Danot, M., 2002, Catal. Today, 28, 23-30.
[11] Sie, S.T., 2003, Ind. Eng. Chem. Res., 31, 1881-1889.
[12] Nurhadi, M., Trisunaryanti, W., Setiaji, B., dan Utoro, Y., 2001, Indo.J. Chem., 1, 1, 7-10.
DOI: https://doi.org/10.22146/ijc.21589
Article Metrics
Abstract views : 2942
| 
views : 4082
Copyright (c) 2010 Indonesian Journal of Chemistry
This work is licensed under a Creative Commons Attribution-NonCommercial-NoDerivatives 4.0 International License.
Indonesian Journal of Chemistry (ISSN 1411-9420 /e-ISSN 2460-1578) - Chemistry Department, Universitas Gadjah Mada, Indonesia.