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铱-雷奥/锐钛矿-TiO 催化剂上赤藓糖醇的选择性加氢。

Selective Hydrogenolysis of Erythritol over Ir-ReO /Rutile-TiO Catalyst.

机构信息

Department of Applied Chemistry, School of Engineering, Tohoku University, 6-6-07, Aoba, Aramaki, Aoba-ku, Sendai, 980-8579, Japan.

College of Environmental Science and Engineering, Institute of New Rural Development, Tongji University, 1239 Siping Road, Shanghai, 200092, P. R. China.

出版信息

ChemSusChem. 2021 Jan 21;14(2):642-654. doi: 10.1002/cssc.202002357. Epub 2020 Nov 4.

Abstract

Partial hydrogenolysis of erythritol, which can be produced at large scale by fermentation, to 1,4-butanediol (1,4-BuD) is investigated with Ir-ReO /SiO and Ir-ReO /rutile-TiO catalysts. In addition to the higher conversion rate over Ir-ReO /TiO than over Ir-ReO /SiO , which has been also reported for glycerol hydrogenolysis, Ir-ReO /TiO showed higher selectivity to 1,4-BuD than Ir-ReO /SiO , especially at low conversion levels, leading to high 1,4-BuD productivity of 20 mmol  g  h at 373 K (36 % conversion, 33 % selectivity). The productivity based on the noble metal amount is higher than those reported previously, although the maximum yield of 1,4-BuD (23 %) is not higher than the highest reported values. The reactions of various triols, diols and mono-ols are tested and the selectivity and the reaction rates are compared between catalysts and between substrates. The Ir-ReO /TiO catalyst showed about twofold higher activity than Ir-ReO /SiO in hydrogenolysis of the C-OH bond at the 2- or 3-positions in 1,2- and 1,3-diols, respectively, whereas the hydrogenolysis of C-OH at the 1-position is less promoted by the TiO support. Lowering the loading amount of Ir on TiO (from 4 wt % to 2 or 1 wt %) decreases the Ir-based activity and 1,4-BuD selectivity. Similarly, increasing the loading amount on SiO from 4 wt % to 20 wt % increases the Ir-based activity and 1,4-BuD selectivity, although they remain lower than those for TiO -supported catalyst with 4 wt % Ir. High metal loadings on the support seem to be important.

摘要

用 Ir-ReO/SiO 和 Ir-ReO/金红石-TiO 催化剂研究了通过发酵大规模生产的赤藓糖醇的部分氢化反应,生成 1,4-丁二醇(1,4-BuD)。除了 Ir-ReO/TiO 相对于 Ir-ReO/SiO 的转化率更高,这在甘油的氢化反应中也有报道,Ir-ReO/TiO 对 1,4-BuD 的选择性也高于 Ir-ReO/SiO ,特别是在低转化率水平下,导致在 373 K(36%转化率,33%选择性)时的 1,4-BuD 高生产率为 20mmol g-1 h-1。基于贵金属的量的生产率高于以前报道的生产率,尽管 1,4-BuD 的最大产量(23%)并不高于报道的最高值。测试了各种三醇、二醇和单醇的反应,比较了催化剂之间和底物之间的选择性和反应速率。与 Ir-ReO/SiO 相比,Ir-ReO/TiO 催化剂在 1,2-和 1,3-二醇中 2 位或 3 位的 C-OH 键的氢化反应中表现出约两倍的活性,而 TiO 载体对 1 位的 C-OH 氢化反应的促进作用较小。降低 TiO 上 Ir 的负载量(从 4wt%降至 2 或 1wt%)会降低基于 Ir 的活性和 1,4-BuD 选择性。同样,将 SiO 上的负载量从 4wt%增加到 20wt%会增加基于 Ir 的活性和 1,4-BuD 选择性,尽管它们仍然低于具有 4wt%Ir 的 TiO 负载催化剂。高金属负载量在载体上似乎很重要。

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