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Nickel-Lanthanum Impregnated into Natural Zeolite as a Catalyst for Biofuel Production from Sunflower Oil via Hydrocracking Process

Bulletin of Chemical Reaction Engineering & Catalysis · Vol. ume (2026) · pp. 68–79

DOI
10.9767/bcrec.20503
ISSN
1978-2993
Published
2026-04-30
Publisher
Masyarakat Katalis Indonesia - Indonesian Catalyst Society (MKICS)
Language
eng
License
creativecommons.org/licenses/by-sa/4.0

Abstract

The increasing demand for crude oil or fossil fuel as a raw material for oil fuel has been steadily rising over time in line with the development that is taking place in Indonesia. However, biofuels are potential vegetable fuels that can be developed as alternative energy because they are renewable and can be renewed to overcome the energy crisis in the future. For this purpose, a double metal catalyst (impregnated with nickel and lanthanum), is used to make biofuels from sunflower seed oil. The effect of metal ratio on the yield of biofuel products is the concern in this study. The temperature of hydrocracking process was 250-330 ℃ with ratio of metal 5% and 10% (metal ratio 1:1 and 1:2). X-ray diffraction (XRD) shows that natural zeolite has a clinoptilolite phase, X-Ray Fluorescence (XRF) shows that acid and base activation increases the Si/Al ratio from 4.5 to 5, Scanning Electron Microscope – Energy Dispersive X-Ray (SEM-EDX) shows images of natural zeolite surfaces in the form of aggregate pieces, and Brunauer Emmett Teller (BET) shows that acid and base activation increases SBET from 29.96 to 49.73 m2/g and forms a hierarchical natural zeolite. The impregnation of Ni-La/Zeolite catalyst has been successfully carried out using the incipient wetness impregnation method and the best catalyst results were obtained, namely Ni-La/Zeolite 10% (1:2) with a surface area of 15.33 m2/gS. The addition of Nickel and Lanthanum metals caused a decrease in the surface area and average pore diameter of the zeolite. The lowest surface area and average pore diameter were found in the variation of the Ni-La/Zeolite 10% (1:2) catalyst, namely 15.33 m2/g and 13.99 nm. The highest hydrocarbon yield was found in the hydrocracking process with the Ni-La/Zeolite 10% (1:1) catalyst with gasoline, kerosene and gasoil fractions of 0.91; 0.39 and 8.32 (%wt), respectively. The hydrocarbon compound composition of the catalyst includes n-paraffin 4.43%, isoparaffin 0.21%, cycloparaffin 2.99% and olefin 2.71%. Copyright © 2026 by Authors, Published by BCREC Publishing Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0).

Keywords

Collaboration network of the authors

40 authors · 133 co-authorship links · 1 across different organisations · showing the 40 most connected

Hover or tap a name to highlight its co-authors. Double-click to open the author's page.

  • Sebelas Maret University
  • Tadulako University
  • National Research and Innovation Agency
  • Hasanuddin University
  • Yogyakarta State University
  • Affiliation unknown
  • Different organisations
  • Same organisation
  • Affiliation unknown
  • Thicker line = more joint articles · bigger circle = more articles
Show as table
Co-authorOrganisationJoint articles
Maja Pranata MarbunAffiliation unknown13
Achmad RoesyadiAffiliation unknown8
Kususanto Ditto PrihadiAffiliation unknown6
Nino RinaldiAffiliation unknown5
Danawati Hari PrajitnoAffiliation unknown5
Hasanudin HasanudinAffiliation unknown4
Muhammad RidwanHasanuddin University3
D. M. Magdalena RitongaAffiliation unknown2
Yan NurcahyaAffiliation unknown2
Novia NoviaTadulako University2
Roni MaryanaAffiliation unknown2
Wan Ryan AsriAffiliation unknown2
Fitri HadiahAffiliation unknown2
Vera PermatasariNational Research and Innovation Agency2
Zahari IshakAffiliation unknown2
Mujtahid MujtahidAffiliation unknown2
Mohammad PadilAffiliation unknown2
Astrid Noviana ParadhitaSebelas Maret University1
Mutiara Auliya KhadijaSebelas Maret University1
Agus PurbayuSebelas Maret University1
Sahirul Alim Tri BawonoSebelas Maret University1
Sri HaryatiSebelas Maret University1
Daaniis Raditya Pramoda WardaniSebelas Maret University1
Rafael Kurniawan Albyseptra PratamaSebelas Maret University1
Diana ZuhrohAffiliation unknown1
Wahyu LestariYogyakarta State University1
Sunarto SunartoAffiliation unknown1
Eko SugiartoAffiliation unknown1
Muh Fakhrihun NaamAffiliation unknown1
Dwi Ardi Wicaksana PutraAffiliation unknown1

Affiliations come from OpenAlex; journal OAI-PMH metadata carries none. Authors without an OpenAlex ID are matched by name, which can merge or split people.

Metadata source: OAI-PMH (metadata jurnal) https://journal.bcrec.id/index.php/bcrec/oai, first harvested 8 Nov 2026, last seen 8 Nov 2026.
Original metadata (oai_dc)
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	<dc:title xml:lang="en-US">Nickel-Lanthanum Impregnated into Natural Zeolite as a Catalyst for Biofuel Production from Sunflower Oil via Hydrocracking Process</dc:title>
	<dc:creator>Santiko, Erik Budi</dc:creator>
	<dc:creator>Fauziah, Sarah</dc:creator>
	<dc:creator>Priyanto, Sugeng</dc:creator>
	<dc:creator>Yustinah, Yustinah</dc:creator>
	<dc:creator>Marlinda, Lenny</dc:creator>
	<dc:creator>Sudibyo, Sudibyo</dc:creator>
	<dc:creator>Aziz, Abdul</dc:creator>
	<dc:creator>Oktiarmi, Peri</dc:creator>
	<dc:creator>Yati, Indri</dc:creator>
	<dc:creator>Al Muttaqii, Muhammad</dc:creator>
	<dc:subject xml:lang="en-US">Nickel-Lanthanum; Natural zeolite; Sunflower oil; Hydrocracking; Green Diesel</dc:subject>
	<dc:description xml:lang="en-US">The increasing demand for crude oil or fossil fuel as a raw material for oil fuel has been steadily rising over time in line with the development that is taking place in Indonesia. However, biofuels are potential vegetable fuels that can be developed as alternative energy because they are renewable and can be renewed to overcome the energy crisis in the future. For this purpose, a double metal catalyst (impregnated with nickel and lanthanum), is used to make biofuels from sunflower seed oil. The effect of metal ratio on the yield of biofuel products is the concern in this study. The temperature of hydrocracking process was 250-330 ℃ with ratio of metal 5% and 10% (metal ratio 1:1 and 1:2). X-ray diffraction (XRD) shows that natural zeolite has a clinoptilolite phase, X-Ray Fluorescence (XRF) shows that acid and base activation increases the Si/Al ratio from 4.5 to 5, Scanning Electron Microscope – Energy Dispersive X-Ray (SEM-EDX) shows images of natural zeolite surfaces in the form of aggregate pieces, and Brunauer Emmett Teller (BET) shows that acid and base activation increases SBET from 29.96 to 49.73 m2/g and forms a hierarchical natural zeolite. The impregnation of Ni-La/Zeolite catalyst has been successfully carried out using the incipient wetness impregnation method and the best catalyst results were obtained, namely Ni-La/Zeolite 10% (1:2) with a surface area of 15.33 m2/gS. The addition of Nickel and Lanthanum metals caused a decrease in the surface area and average pore diameter of the zeolite. The lowest surface area and average pore diameter were found in the variation of the Ni-La/Zeolite 10% (1:2) catalyst, namely 15.33 m2/g and 13.99 nm. The highest hydrocarbon yield was found in the hydrocracking process with the Ni-La/Zeolite 10% (1:1) catalyst with gasoline, kerosene and gasoil fractions of 0.91; 0.39 and 8.32 (%wt), respectively. The hydrocarbon compound composition of the catalyst includes n-paraffin 4.43%, isoparaffin 0.21%, cycloparaffin 2.99% and olefin 2.71%. Copyright © 2026 by Authors, Published by BCREC Publishing Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0).</dc:description>
	<dc:publisher xml:lang="en-US">Masyarakat Katalis Indonesia - Indonesian Catalyst Society (MKICS)</dc:publisher>
	<dc:date>2026-04-30</dc:date>
	<dc:type>info:eu-repo/semantics/article</dc:type>
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	<dc:format>application/pdf</dc:format>
	<dc:identifier>https://journal.bcrec.id/index.php/bcrec/article/view/20503</dc:identifier>
	<dc:identifier>10.9767/bcrec.20503</dc:identifier>
	<dc:source xml:lang="en-US">Bulletin of Chemical Reaction Engineering &amp; Catalysis; 2026: BCREC Volume 21 Issue 1 Year 2026 (April 2026); 68-79</dc:source>
	<dc:source>1978-2993</dc:source>
	<dc:language>eng</dc:language>
	<dc:relation>https://journal.bcrec.id/index.php/bcrec/article/view/20503/9872</dc:relation>
	<dc:rights xml:lang="en-US">Copyright (c) 2026 by Authors, Published by BCREC Publishing Group</dc:rights>
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