Selective Hydrogenation of Stearic Acid to 1-Octadecanol Using Bimetallic Palladium-Tin Supported on Carbon Catalysts at Mild Reaction Conditions
IF 1.3
Q3 ENGINEERING, CHEMICAL
Rodiansono Rodiansono, Elisa Hayati, Atina Sabila Azzahra, M. Astuti, K. Mustikasari, S. Husain, S. Sutomo
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Abstract
Bimetallic palladium-tin catalysts supported on microporous carbon (denoted as Pd-Sn(x)/C, loading amount of Pd = 5 wt% and x = Pd/Sn molar ratio; c.a. 3.0; 1.5; and 1.0) showed high selectivity in the hydrogenation of stearic acid towards 1-octadecanol (stearyl alcohol) under mild reaction conditions. Pd-Sn(x)/C catalysts were synthesized via the hydrothermal method at temperature of 150 °C for 24 h, and reduced with H2 at 400 °C for 3 h. Pd-Sn(1.5)/C catalyst exhibited the highest yield of stearyl alcohol (1-octadecanol) (up to 73.2%) at 100% conversion of stearic acid at temperature 240 °C, initial H2 pressure of 3.0 MPa, a reaction time of 13 h, and in 2-propanol/water solvent. The high selectivity of alcohols over Pd-Sn(1.5)/C catalyst can be attributed to the formation of bimetallic Pd-Sn alloy phases (e.g. Pd3Sn and Pd3Sn2) as obviously depicted by XRD analysis. The presence of co-promotor Sn and the formation of bimetallic may play a pivotal role in the high selectivity of 1-octadecanol. Copyright © 2021 by Authors, Published by BCREC Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0).
碳负载双金属钯锡在温和反应条件下选择性加氢硬脂酸制1-十八醇
负载在微孔碳上的双金属钯-锡催化剂(表示为Pd-Sn(x)/C,Pd的负载量=5wt%和x=Pd/Sn摩尔比;c.a.3.0;1.5;和1.0)在温和的反应条件下显示出硬脂酸对1-十八醇(硬脂醇)的氢化的高选择性。在150°C的温度下,通过水热法合成了Pd-Sn(x)/C催化剂24小时,并在400°C下用H2还原3小时。在240°C、初始H2压力为3.0MPa、反应时间为13小时和2-丙醇/水溶剂中,当硬脂酸转化率为100%时,Pd-Sn(1.5)/C催化剂表现出最高的硬脂醇(1-十八醇)产率(高达73.2%)。醇在Pd-Sn(1.5)/C催化剂上的高选择性可归因于双金属Pd-Sn合金相(例如Pd3Sn和Pd3Sn2)的形成,如XRD分析所示。助催化剂Sn的存在和双金属的形成可能对1-十八醇的高选择性起着关键作用。版权所有©2021作者所有,BCREC集团出版。这是CC BY-SA许可证下的开放访问文章(https://creativecommons.org/licenses/by-sa/4.0)。
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期刊介绍:
Bulletin of Chemical Reaction Engineering & Catalysis, a reputable international journal, provides a forum for publishing the novel technologies related to the catalyst, catalysis, chemical reactor, kinetics, and chemical reaction engineering. Scientific articles dealing with the following topics in chemical reaction engineering, catalysis science and engineering, catalyst preparation method and characterization, novel innovation of chemical reactor, kinetic studies, etc. are particularly welcome. However, articles concerned on general chemical engineering process are not covered and out of scope of this journal