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...
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Diponegoro University
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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 >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 & 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 >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 & 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 |
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