Effect of Co and Mo Metal Addition in Co-Mo / Zeolite Y Catalyst for Coal Tar Conversion to Liquid Fuel

Coal tar can be used as an alternative source for the production of conventional liquid fuels such as gasoline and diesel, through the process of hydrogenation/ hydrocracking. This research is aimed to investigate the effect of Co and Mo in Co-Mo / zeolite Y catalyst in liquid fuel production from c...

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Main Authors: D.D. Anggoro, L. Buchori, T. Friandani, Z.R. Ramadhan
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2017-03-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/1698
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spelling doaj-ed2323feca35447c89306b618b9d375d2021-02-18T21:08:26ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162017-03-015610.3303/CET1756287Effect of Co and Mo Metal Addition in Co-Mo / Zeolite Y Catalyst for Coal Tar Conversion to Liquid FuelD.D. AnggoroL. BuchoriT. FriandaniZ.R. RamadhanCoal tar can be used as an alternative source for the production of conventional liquid fuels such as gasoline and diesel, through the process of hydrogenation/ hydrocracking. This research is aimed to investigate the effect of Co and Mo in Co-Mo / zeolite Y catalyst in liquid fuel production from coal tar. The catalyst was prepared via wet impregnation. The objectives of this research are to determine the effect of the addition Co and Mo metals on liquid fuel production process from coal tar, and to know the characteristics of the catalysts by impregnation method. This study began with the preparation of Co-Mo / zeolite Y catalyst, followed by the hydrocracking / hydrotreating reaction between coal tar with hydrogen gases. The independent variables (weight cobalt metals and molybdenum metals) were optimised to obtain the optimum liquid fuels yield. The characterisation results indicated that the increasing concentration of Co and Mo caused the decreasing in the surface area of the catalyst. The acidity of catalysts changed with loaded Co and Mo to zeolite Y. Results of SEM and XRD analysis showed that the morphology and crystal form of Co-Mo / zeolite Y unchanged with zeolite Y before impregnated with Co and Mo. Optimum liquid fuel yield (1.80 %) was obtained on a composition weight with Co metal of 0.59 g and Mo metal of 0.5 g.https://www.cetjournal.it/index.php/cet/article/view/1698
collection DOAJ
language English
format Article
sources DOAJ
author D.D. Anggoro
L. Buchori
T. Friandani
Z.R. Ramadhan
spellingShingle D.D. Anggoro
L. Buchori
T. Friandani
Z.R. Ramadhan
Effect of Co and Mo Metal Addition in Co-Mo / Zeolite Y Catalyst for Coal Tar Conversion to Liquid Fuel
Chemical Engineering Transactions
author_facet D.D. Anggoro
L. Buchori
T. Friandani
Z.R. Ramadhan
author_sort D.D. Anggoro
title Effect of Co and Mo Metal Addition in Co-Mo / Zeolite Y Catalyst for Coal Tar Conversion to Liquid Fuel
title_short Effect of Co and Mo Metal Addition in Co-Mo / Zeolite Y Catalyst for Coal Tar Conversion to Liquid Fuel
title_full Effect of Co and Mo Metal Addition in Co-Mo / Zeolite Y Catalyst for Coal Tar Conversion to Liquid Fuel
title_fullStr Effect of Co and Mo Metal Addition in Co-Mo / Zeolite Y Catalyst for Coal Tar Conversion to Liquid Fuel
title_full_unstemmed Effect of Co and Mo Metal Addition in Co-Mo / Zeolite Y Catalyst for Coal Tar Conversion to Liquid Fuel
title_sort effect of co and mo metal addition in co-mo / zeolite y catalyst for coal tar conversion to liquid fuel
publisher AIDIC Servizi S.r.l.
series Chemical Engineering Transactions
issn 2283-9216
publishDate 2017-03-01
description Coal tar can be used as an alternative source for the production of conventional liquid fuels such as gasoline and diesel, through the process of hydrogenation/ hydrocracking. This research is aimed to investigate the effect of Co and Mo in Co-Mo / zeolite Y catalyst in liquid fuel production from coal tar. The catalyst was prepared via wet impregnation. The objectives of this research are to determine the effect of the addition Co and Mo metals on liquid fuel production process from coal tar, and to know the characteristics of the catalysts by impregnation method. This study began with the preparation of Co-Mo / zeolite Y catalyst, followed by the hydrocracking / hydrotreating reaction between coal tar with hydrogen gases. The independent variables (weight cobalt metals and molybdenum metals) were optimised to obtain the optimum liquid fuels yield. The characterisation results indicated that the increasing concentration of Co and Mo caused the decreasing in the surface area of the catalyst. The acidity of catalysts changed with loaded Co and Mo to zeolite Y. Results of SEM and XRD analysis showed that the morphology and crystal form of Co-Mo / zeolite Y unchanged with zeolite Y before impregnated with Co and Mo. Optimum liquid fuel yield (1.80 %) was obtained on a composition weight with Co metal of 0.59 g and Mo metal of 0.5 g.
url https://www.cetjournal.it/index.php/cet/article/view/1698
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