Catalytic Hydrogenation of Levulinic Acid in Water into g-Valerolactone over Bulk Structure of Inexpensive Intermetallic Ni-Sn Alloy Catalysts

<p>A bulk structure of inexpensive intermetallic nickel-tin (Ni-Sn) alloys catalysts demonstrated highly selective in the hydrogenation of levulinic acid in water into g-valerolactone. The intermetallic Ni-Sn catalysts were synthesized via a very simple thermochemical method from non-organomet...

Full description

Bibliographic Details
Main Authors: Rodiansono Rodiansono, Maria Dewi Astuti, Abdul Ghofur, Kiky C. Sembiring
Format: Article
Language:English
Published: Diponegoro University 2015-07-01
Series:Bulletin of Chemical Reaction Engineering & Catalysis
Subjects:
Online Access:http://ejournal.undip.ac.id/index.php/bcrec/article/view/8284
id doaj-49159ec3c0ca43d1a1eebee6239424d7
record_format Article
spelling doaj-49159ec3c0ca43d1a1eebee6239424d72020-11-24T22:54:24ZengDiponegoro UniversityBulletin of Chemical Reaction Engineering & Catalysis1978-29932015-07-0110219220010.9767/bcrec.10.2.8284.192-2007204Catalytic Hydrogenation of Levulinic Acid in Water into g-Valerolactone over Bulk Structure of Inexpensive Intermetallic Ni-Sn Alloy CatalystsRodiansono Rodiansono0Maria Dewi Astuti1Abdul Ghofur2Kiky C. Sembiring3Department of Chemistry, Lambung Mangkurat University, Jl. A. Yani Km 36, Banjarbaru,Department of Chemistry, Lambung Mangkurat University, Jl. A. Yani Km 36, Banjarbaru,Department of Environmental Engineering, Lambung Mangkurat University, Jl. A. Yani Km 35.6 BanjarbaruResearch Centre for Chemistry, Indonesian Institute of Sciences, Puspiptek Serpong, Tangerang<p>A bulk structure of inexpensive intermetallic nickel-tin (Ni-Sn) alloys catalysts demonstrated highly selective in the hydrogenation of levulinic acid in water into g-valerolactone. The intermetallic Ni-Sn catalysts were synthesized via a very simple thermochemical method from non-organometallic precursor at low temperature followed by hydrogen treatment at 673 K for 90 min. The molar ratio of nickel salt and tin salt was varied to obtain the corresponding Ni/Sn ratio of 4.0, 3.0, 2.0, 1.5, and 0.75. The formation of Ni-Sn alloy species was mainly depended on the composition and temperature of H<sub>2</sub> treatment. Intermetallics Ni-Sn that contain Ni<sub>3</sub>Sn, Ni<sub>3</sub>Sn<sub>2</sub>, and Ni<sub>3</sub>Sn<sub>4</sub> alloy phases are known to be effective heterogeneous catalysts for levulinic acid hydrogenation giving very excellence g-valerolactone yield of &gt;99% at 433 K, initial H<sub>2</sub> pressure of 4.0 MPa within 6 h. The effective hydrogenation was obtained in H<sub>2</sub>O without the formation of by-product. Intermetallic Ni-Sn(1.5) that contains Ni<sub>3</sub>Sn<sub>2</sub> alloy species demonstrated very stable and reusable catalyst without any significant loss of its selectivity. © 2015 BCREC UNDIP. All rights reserved.</p> <p><em>Received: 26th February 2015; Revised: 16th April 2015; Accepted: 22nd April 2015</em></p> <p> </p><p><strong>How to Cite</strong>: Rodiansono, R., Astuti, M.D., Ghofur, A., Sembiring, K.C. (2015). Catalytic Hydrogenation of Levulinic Acid in Water into g-Valerolactone over Bulk Structure of Inexpensive Intermetallic Ni-Sn Alloy Catalysts. <em>Bulletin of Chemical Reaction Engineering &amp; Catalysis</em>, 10 (2): 192-200. (doi:10.9767/bcrec.10.2.8284.192-200)</p><p><strong>Permalink/DOI</strong>: http://dx.doi.org/10.9767/bcrec.10.2.8284.192-200</p> <p> </p>http://ejournal.undip.ac.id/index.php/bcrec/article/view/8284intermetallic nickel tinNi3SnNi3Sn2Ni3Sn4levulinic acidg-valerolactonehydrogenation
collection DOAJ
language English
format Article
sources DOAJ
author Rodiansono Rodiansono
Maria Dewi Astuti
Abdul Ghofur
Kiky C. Sembiring
spellingShingle Rodiansono Rodiansono
Maria Dewi Astuti
Abdul Ghofur
Kiky C. Sembiring
Catalytic Hydrogenation of Levulinic Acid in Water into g-Valerolactone over Bulk Structure of Inexpensive Intermetallic Ni-Sn Alloy Catalysts
Bulletin of Chemical Reaction Engineering & Catalysis
intermetallic nickel tin
Ni3Sn
Ni3Sn2
Ni3Sn4
levulinic acid
g-valerolactone
hydrogenation
author_facet Rodiansono Rodiansono
Maria Dewi Astuti
Abdul Ghofur
Kiky C. Sembiring
author_sort Rodiansono Rodiansono
title Catalytic Hydrogenation of Levulinic Acid in Water into g-Valerolactone over Bulk Structure of Inexpensive Intermetallic Ni-Sn Alloy Catalysts
title_short Catalytic Hydrogenation of Levulinic Acid in Water into g-Valerolactone over Bulk Structure of Inexpensive Intermetallic Ni-Sn Alloy Catalysts
title_full Catalytic Hydrogenation of Levulinic Acid in Water into g-Valerolactone over Bulk Structure of Inexpensive Intermetallic Ni-Sn Alloy Catalysts
title_fullStr Catalytic Hydrogenation of Levulinic Acid in Water into g-Valerolactone over Bulk Structure of Inexpensive Intermetallic Ni-Sn Alloy Catalysts
title_full_unstemmed Catalytic Hydrogenation of Levulinic Acid in Water into g-Valerolactone over Bulk Structure of Inexpensive Intermetallic Ni-Sn Alloy Catalysts
title_sort catalytic hydrogenation of levulinic acid in water into g-valerolactone over bulk structure of inexpensive intermetallic ni-sn alloy catalysts
publisher Diponegoro University
series Bulletin of Chemical Reaction Engineering & Catalysis
issn 1978-2993
publishDate 2015-07-01
description <p>A bulk structure of inexpensive intermetallic nickel-tin (Ni-Sn) alloys catalysts demonstrated highly selective in the hydrogenation of levulinic acid in water into g-valerolactone. The intermetallic Ni-Sn catalysts were synthesized via a very simple thermochemical method from non-organometallic precursor at low temperature followed by hydrogen treatment at 673 K for 90 min. The molar ratio of nickel salt and tin salt was varied to obtain the corresponding Ni/Sn ratio of 4.0, 3.0, 2.0, 1.5, and 0.75. The formation of Ni-Sn alloy species was mainly depended on the composition and temperature of H<sub>2</sub> treatment. Intermetallics Ni-Sn that contain Ni<sub>3</sub>Sn, Ni<sub>3</sub>Sn<sub>2</sub>, and Ni<sub>3</sub>Sn<sub>4</sub> alloy phases are known to be effective heterogeneous catalysts for levulinic acid hydrogenation giving very excellence g-valerolactone yield of &gt;99% at 433 K, initial H<sub>2</sub> pressure of 4.0 MPa within 6 h. The effective hydrogenation was obtained in H<sub>2</sub>O without the formation of by-product. Intermetallic Ni-Sn(1.5) that contains Ni<sub>3</sub>Sn<sub>2</sub> alloy species demonstrated very stable and reusable catalyst without any significant loss of its selectivity. © 2015 BCREC UNDIP. All rights reserved.</p> <p><em>Received: 26th February 2015; Revised: 16th April 2015; Accepted: 22nd April 2015</em></p> <p> </p><p><strong>How to Cite</strong>: Rodiansono, R., Astuti, M.D., Ghofur, A., Sembiring, K.C. (2015). Catalytic Hydrogenation of Levulinic Acid in Water into g-Valerolactone over Bulk Structure of Inexpensive Intermetallic Ni-Sn Alloy Catalysts. <em>Bulletin of Chemical Reaction Engineering &amp; Catalysis</em>, 10 (2): 192-200. (doi:10.9767/bcrec.10.2.8284.192-200)</p><p><strong>Permalink/DOI</strong>: http://dx.doi.org/10.9767/bcrec.10.2.8284.192-200</p> <p> </p>
topic intermetallic nickel tin
Ni3Sn
Ni3Sn2
Ni3Sn4
levulinic acid
g-valerolactone
hydrogenation
url http://ejournal.undip.ac.id/index.php/bcrec/article/view/8284
work_keys_str_mv AT rodiansonorodiansono catalytichydrogenationoflevulinicacidinwaterintogvalerolactoneoverbulkstructureofinexpensiveintermetallicnisnalloycatalysts
AT mariadewiastuti catalytichydrogenationoflevulinicacidinwaterintogvalerolactoneoverbulkstructureofinexpensiveintermetallicnisnalloycatalysts
AT abdulghofur catalytichydrogenationoflevulinicacidinwaterintogvalerolactoneoverbulkstructureofinexpensiveintermetallicnisnalloycatalysts
AT kikycsembiring catalytichydrogenationoflevulinicacidinwaterintogvalerolactoneoverbulkstructureofinexpensiveintermetallicnisnalloycatalysts
_version_ 1725660081110908928