Selectivity of an Active Natural Zeolite in Catalytic Conversion Process of <i>Bangkirai, Kruing</i> and <i>Kamper</i> Woods Biofuel to Gasoline Fraction
The selectivity of an active natural zeolite (ZAAH) in catalytic conversion process of Bangkirai, Kruing and Kamper woods biofuels has been studied. The ZAAH catalyst was prepared from a natural zeolite (ZA) treated with acids solution (1% HF and 6M HCI) and hydrothermal then calcined at 500 °C and...
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doaj-ac7cbe18244d42bf8e659283f2e5c81b2020-11-24T22:03:15ZengUniversitas Gadjah MadaIndonesian Journal of Chemistry1411-94202460-15782010-06-0111354210.22146/ijc.2195915057Selectivity of an Active Natural Zeolite in Catalytic Conversion Process of <i>Bangkirai, Kruing</i> and <i>Kamper</i> Woods Biofuel to Gasoline FractionWega Trisunaryanti0Department of Chemistry, Faculty of Mathematics and Natural Sciences, Universitas Gadjah Mada, Sekip Utara PO BOX BLS 21, Yogyakarta 55281The selectivity of an active natural zeolite (ZAAH) in catalytic conversion process of Bangkirai, Kruing and Kamper woods biofuels has been studied. The ZAAH catalyst was prepared from a natural zeolite (ZA) treated with acids solution (1% HF and 6M HCI) and hydrothermal then calcined at 500 °C and oxidized at 400 °C under nitrogen and oxygen gas stream, respectively. Characterizations of the catalysts including Si/Al ratio and acidity were determined by atomic adsorption spectroscopy (AAS) and ammonia gas adsorption method, respectively. The conversion process was carried out in a flow reactor system at 400 °C, under N2 stream (20 mL/min). The biofuel was vaporized from the pyrolysis zone to the catalytic reactor. A liquid product was covered and analyzed by gas chromatograph (GC) and that connected with mass spectroscopy (GC-MS). The characterization results showed that the Si/AI ratio and acidity of the ZAAH were higher than that of the ZA catalyst. The GC-MS data showed that the highest product selectivity was 2,4-dimethyl heptane and 1,2-dimethyl benzene. The total product selectivity using the ZAAH catalyst (bangkirai = 68.10%; kruing = 54.76%; kamper = 50.72%) was higher than that of the ZA catalyst (bangkirai = 39.24%; kruing = 44.38%; kamper = 46.11%).https://jurnal.ugm.ac.id/ijc/article/view/21959active natural zeoliteselectivitybiofuelgasoline fraction |
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DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Wega Trisunaryanti |
spellingShingle |
Wega Trisunaryanti Selectivity of an Active Natural Zeolite in Catalytic Conversion Process of <i>Bangkirai, Kruing</i> and <i>Kamper</i> Woods Biofuel to Gasoline Fraction Indonesian Journal of Chemistry active natural zeolite selectivity biofuel gasoline fraction |
author_facet |
Wega Trisunaryanti |
author_sort |
Wega Trisunaryanti |
title |
Selectivity of an Active Natural Zeolite in Catalytic Conversion Process of <i>Bangkirai, Kruing</i> and <i>Kamper</i> Woods Biofuel to Gasoline Fraction |
title_short |
Selectivity of an Active Natural Zeolite in Catalytic Conversion Process of <i>Bangkirai, Kruing</i> and <i>Kamper</i> Woods Biofuel to Gasoline Fraction |
title_full |
Selectivity of an Active Natural Zeolite in Catalytic Conversion Process of <i>Bangkirai, Kruing</i> and <i>Kamper</i> Woods Biofuel to Gasoline Fraction |
title_fullStr |
Selectivity of an Active Natural Zeolite in Catalytic Conversion Process of <i>Bangkirai, Kruing</i> and <i>Kamper</i> Woods Biofuel to Gasoline Fraction |
title_full_unstemmed |
Selectivity of an Active Natural Zeolite in Catalytic Conversion Process of <i>Bangkirai, Kruing</i> and <i>Kamper</i> Woods Biofuel to Gasoline Fraction |
title_sort |
selectivity of an active natural zeolite in catalytic conversion process of <i>bangkirai, kruing</i> and <i>kamper</i> woods biofuel to gasoline fraction |
publisher |
Universitas Gadjah Mada |
series |
Indonesian Journal of Chemistry |
issn |
1411-9420 2460-1578 |
publishDate |
2010-06-01 |
description |
The selectivity of an active natural zeolite (ZAAH) in catalytic conversion process of Bangkirai, Kruing and Kamper woods biofuels has been studied. The ZAAH catalyst was prepared from a natural zeolite (ZA) treated with acids solution (1% HF and 6M HCI) and hydrothermal then calcined at 500 °C and oxidized at 400 °C under nitrogen and oxygen gas stream, respectively. Characterizations of the catalysts including Si/Al ratio and acidity were determined by atomic adsorption spectroscopy (AAS) and ammonia gas adsorption method, respectively. The conversion process was carried out in a flow reactor system at 400 °C, under N2 stream (20 mL/min). The biofuel was vaporized from the pyrolysis zone to the catalytic reactor. A liquid product was covered and analyzed by gas chromatograph (GC) and that connected with mass spectroscopy (GC-MS). The characterization results showed that the Si/AI ratio and acidity of the ZAAH were higher than that of the ZA catalyst. The GC-MS data showed that the highest product selectivity was 2,4-dimethyl heptane and 1,2-dimethyl benzene. The total product selectivity using the ZAAH catalyst (bangkirai = 68.10%; kruing = 54.76%; kamper = 50.72%) was higher than that of the ZA catalyst (bangkirai = 39.24%; kruing = 44.38%; kamper = 46.11%). |
topic |
active natural zeolite selectivity biofuel gasoline fraction |
url |
https://jurnal.ugm.ac.id/ijc/article/view/21959 |
work_keys_str_mv |
AT wegatrisunaryanti selectivityofanactivenaturalzeoliteincatalyticconversionprocessofibangkiraikruingiandikamperiwoodsbiofueltogasolinefraction |
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