Martin Muhler studied chemistry at the Ludwig-Maximilians-Universität in Munich from 1980 to 1986. He moved to Berlin to the Fritz-Haber-Institute of the Max-Planck-Society (FHI) joining Prof. Dr. G. Ertl’s group as PhD student. He received his PhD in 1989 from the Freie Universität Berlin. He joined Haldor Topsoe A/S in Denmark as a postdoctoral fellow from 1989 to 1991. He returned to Prof. Ertl’s Department of Physical Chemistry as head of the group “Heterogeneous Catalysis” and finished his habilitation in Industrial Chemistry in 1996 (Technische Universität Berlin). In 1996 he was appointed full professor in Industrial Chemistry at the Ruhr-University Bochum, where he still is.
His research is focused on heterogeneous redox catalysis comprising selective reduction and oxidation, electrocatalysis and photocatalysis. Syngas catalysis is a major topic on which he has been working for more than 20 years. His number of publications is close to 400 (h-index of 51). He is a member of the International Advisory Boards of ChemCatChem, ChemSusChem, and the State Key Laboratory of Catalysis at the DICP in Dalian. He is the German representative in the European Federation of Catalysis Societies (EFCATS) and in the International Association of Catalysis Societies (IACS). Since 2014 he is the Chairman of the German Catalysis Society (GeCatS).
The Max Planck Fellow group “Heterogeneous Redox Catalysis” (<link http: www.techem.rub.de>
) performs fundamental research in the area of heterogeneous redox catalysis in the liquid phase under mild conditions and aims at developing catalysts based on mechanistic insight. The scientific challenge is the elucidation of the reaction mechanisms and the interplay of the reactants with the complex surface chemistry of heterogeneous catalysts on the atomic level. Heterogeneous catalysts usually consist of many phases and components, often present as nanoparticles or as X-ray amorphous layers on bulk supports. For many catalysts the chemical reactivity of supported metallic or oxidic nanoparticles is influenced by strong interactions with the support.The reaction conditions of thermal redox catalysis experiments are chosen at temperatures below 200 °C in the liquid phase to guarantee conservation of the kinetic control of specific materials properties such as defects that have been deliberately adjusted by targeted catalyst synthesis. Reduction catalysis focuses on the hydrodeoxygenation of polyols such as glycerol, whereas oxidation catalysis comprises the selective oxidation of short chain alcohol and the challenging C-H bond activation of hydrocarbons. Low temperatures also exclude the Mars – van Krevelen mechanism by avoiding bulk diffusion of oxygen anions in oxides. In addition to thermal catalysis, electrocatalytic reactions such as the oxygen evolution reaction (OER) and electrochemical alcohol oxidation are also investigated. Liquid phase oxidation and electrocatalysis require a deeper understanding of solvation-related phenomena. Corrosion is a common phenomenon leading to catalyst deactivation or dissolution and re-deposition equilibria.
Glycerol is an attractive biomass feedstock due to its relatively low cost and ample availability as a by-product of biodiesel production. Glycerol can be converted to high value-added oxygenated chemicals such as propanediols via hydrodeoxygenation. The aqueous phase deoxygenation of glycerol to propanediols requires selectively cleaving just one of the C–O bonds, but preserving the C–C bonds. It occurs catalytically on bifunctional catalysts via consecutive dehydration and hydrogenation in the presence of H2 at moderate temperatures and relatively high pressures. By far, catalyst exploration has been mainly focused on noble metal-based catalysts such as Pt/Al2O3,[1,2] and therefore the utilization of low-cost Cu-based catalyst is of high interest.
Oxidation reactions are investigated with molecular oxygen as the preferred oxidant as well as with alternative oxidants such as hydrogen peroxide and tert-butyl hydroperoxide (TBHP) as oxygen donor. Employed catalysts include both precious metal-based catalysts such as Au/TiO2 and Pd/CNT, or base metal oxides such as Co-containing spinels and perovskites. The reactions comprise liquid-phase oxidation of short-chain alcohols,[3,4] the oxidation of biomass-related 5-hydroxymethylfurfural (5-HMF) to 2,5-furan dicarboxylic acid (2,5-FDCA), as well as on the challenging C-H bond activation of aliphatic or aromatic hydrocarbons.
For example, we have recently studied the selective oxidation of ethanol in the liquid phase with Pd nanoparticles supported on carbon nanotubes (CNTs).[4] The characterization of the surface and bulk properties combined with the catalytic tests indicate the dissolution and re-deposition of Pd species under reaction conditions. Nitrogen-doped carbon nanotubes (NCNTs) act as an excellent support for the Pd catalyst system by efficiently stabilizing and recapturing the Pd species resulting in high activity and selectivity to acetic acid.
The abovementioned reactions are primarily performed in the batch mode, that is, reactions in autoclaves (see Figure 1 and 2) to screen the catalysts and to optimize reaction conditions. In addition, continuously operated reactors such as the H-Cube Pro TM system (see Figure 3), having many advantages like higher interfacial area, better mass / heat transfer, safe and easy operation, will be utilized for systematic kinetic studies. In close collaboration with Prof. Dr.-Ing. Marcus Gruenewald in Chemical Engineering at the Ruhr-University Bochum (http://www.fluidvt.rub.de), micro-structured reactors will be developed and operated continuously.
Electrocatalysis combines heterogeneous catalysis and electrochemistry. Thermal and electrochemical processes involving coupled electron and proton transfer and radicals as intermediates can be studied using the same heterogeneous catalyst provided that the support has sufficient electrical conductivity. Electrochemical alcohol oxidation reactions as well as the attractive OER are our main interest in this field, and most measurements are carried out using an electrochemical workstation (see Figure 4). In-depth electrocatalytic studies are performed in close collaboration with Prof. Dr. Wolfgang Schuhmann (http://www.rub.de/elan) at the Ruhr-University Bochum using all state-of-the-art electrochemical methods including nanoelectrodes (scanning electrochemical microscope, SECM).
For example, we have recently demonstrated the improved utilization of palladium as anode catalyst for ethanol oxidation by exploiting the strong interaction between Pd nanoparticles and NCNTs as support [5]. 0.85 wt% Pd/NCNTs achieved a specific current density of 517 A/gPd. The electrocatalytic performance deteriorated only gradually and catalysis was sustained for at least 80 h.
In situ attenuated total reflection infrared spectroscopy (ATR-IR, see Figure 5) is used to investigate reaction mechanisms of liquid-phase redox reactions. ATR-IR is ideally suited for studying molecular vibrations at the solid-liquid interface, because the evanescent wave is restricted to the region near the interface of the internal reflection element, thereby minimizing the contribution from the solvent. The in situ ATR-IR investigation of a heterogeneous solid-liquid catalytic reaction provides information about the catalytic surface and the absorbed species on the catalyst surfaces such as reactants, products, and long-lived intermediates. These investigations are supported by in situ Raman spectroscopy studies in Prof. Schuhmann’s group.
Our research also contributes to the Cluster of Excellence RESOLV (http://www.ruhr-uni-bochum.de/solvation) aiming at a deeper understanding of solvation-related phenomena.
[1] A. Wawrzetz, B. Peng, A. Hrabar, A. Jentys, A. A. Lemonidou, J. A. Lercher, J. Catal. 269 (2010) 411.
[2] B. Peng, C. Zhao, I. Mejía-Centeno, G. A. Fuentes, A. Jentys, J. A. Lercher, Catal. Today 183 (2012) 3.
[3] W. Dong, S. Reichenberger, S. Chu, P. Weide, H. Ruland, S. Barcikowski, P. Wagener, M. Muhler, J. Catal. 330 (2015) 497.
[4] W. Dong, P. Chen, W. Xia, P. Weide, H. Ruland, A. Kostka, K. Köhler, M. Muhler, ChemCatChem (2016) 8, 1269 – 1273.
[5] D. Hiltrop, J. Masa, A. Maljusch, W. Xia, W. Schuhmann, M. Muhler, Electrochemistry Communications 63 (2016) 30.