R. Schomaecker

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Name: R. Schomäcker
Organization: Technical University of Berlin , Germany
Department: Department of Chemistry
Title: (PhD)

TOPICS

Co-reporter:Marcel Schmidt;Burgert Blom;Tibor Szilvási;Reinhard Schomäcker;Matthias Driess
European Journal of Inorganic Chemistry 2017 Volume 2017(Issue 9) pp:1284-1291
Publication Date(Web):2017/03/03
DOI:10.1002/ejic.201700148
For the first time, a significant boost in catalytic activity in the rhodium-catalysed hydroformylation of an alkene by using a bidentate bis(N-heterocyclic silylene) ligand is reported. This is shown by the hydroformylation of styrene at 30 bar CO/H2 pressure in the presence of [HRh(CO)(PPh3)3] with an excess of the ferrocenediyl-based bis-NHSi ligand 4, [({η5-C5H4{PhC(NtBu)2}Si})2Fe], which results in superior catalytic activity, compared with the bidentate diphosphines DPPF (3a) and xantphos (3b). In contrast, the hydroformylation of styrene in the presence of [HRh(CO)(PPh3)3] with excesses of the monodentate NHSi ligands [{PhC(NtBu)2}SiNMe2] (1) and [{C2H2(NtBu)2}Si:] (2) at 30 bar CO/H2 pressure revealed considerably slower conversion to the aldehyde products than [HRh(CO)(PPh3)3], with or without an excess of PPh3, showing catalyst deactivation. Surprisingly, the germanium analogue of 4 is shown to be virtually catalytically inactive. The superior activity of 4, compared with the xantphos-containing benchmark system, is rationalized on the basis of solution NMR spectroscopic studies, and the comparative catalyst cycles are elucidated using density functional theory (DFT) methods. The latter quantum-chemical studies explain very well the favourable energy pathway for the hydroformylation of styrene using 4 versus xantphos.
Co-reporter:Y. Kasaka, B. Bibouche, I. Volovych, M. Schwarze, R. Schomäcker
Colloids and Surfaces A: Physicochemical and Engineering Aspects 2016 Volume 494() pp:49-58
Publication Date(Web):5 April 2016
DOI:10.1016/j.colsurfa.2016.01.013
•Phase behaviour for catalytic reactions in microemulsion systems is investigated.•In hydroformulation reactions, phase boundaries are shifted during reaction.•In Heck reactions, one-phase systems are possible at low reactant concentrations.•High inorganic base concentrations lead to two-phase systems.The phase behaviour of microemulsion systems, which are used as reaction media for hydroformulation and Heck coupling reactions, is investigated. A detailed analysis of microemulsion systems is the key for a successful implementation in technical processes. In the case of the hydroformulation reaction, the desired three-phase state is shifted depending on the composition of the reaction mixture and a temperature profile is required to maintain this state during the whole reaction. In case of the Heck coupling reaction, the desired state is an oil-in-water (o/w) one-phase microemulsion. We found that the best reaction performance is with K2CO3 as the base, but at higher reactant concentrations with the same base only two-phase systems are obtained. Heck reaction was successfully performed at higher reactant concentrations in the two-phase system consisting of >75 wt% water. The applied heterogeneous sol–gel supported palladium catalyst could be easily recycled with minor catalyst leaching.
Co-reporter:M. Yildiz, Y. Aksu, U. Simon, K. Kailasam, O. Goerke, F. Rosowski, R. Schomäcker, A. Thomas and S. Arndt  
Chemical Communications 2014 vol. 50(Issue 92) pp:14440-14442
Publication Date(Web):10 Oct 2014
DOI:10.1039/C4CC06561A
The oxidative coupling of methane is a highly promising reaction for its direct conversion. Silica supported MnxOy–Na2WO4 is a suitable catalyst for this reaction. In this study, a variety of different SiO2 materials have been tested as supports. Surprisingly, the application of ordered mesoporous silicas, here exemplarily shown for SBA-15 as support materials, greatly enhances the catalytic performance. The CH4 conversion increased two fold and also the C2 selectivity is strongly increased.
Co-reporter:Carlos Carrero, Markus Kauer, Arne Dinse, Till Wolfram, Neil Hamilton, Annette Trunschke, Robert Schlögl and Reinhard Schomäcker  
Catalysis Science & Technology 2014 vol. 4(Issue 3) pp:786-794
Publication Date(Web):13 Dec 2013
DOI:10.1039/C3CY00625E
Grafted VxOy catalysts for oxidative dehydrogenation of propane (ODP) have been studied due to their potential high performance and as model catalysts in the past. We report on a positive synergetic effect capable of considerably enhancing the propene productivities above reported performances. The most productive catalysts were found at metal loadings (V + Ti) close to the monolayer coverage. The 4V/13Ti/SBA-15 catalyst presented a considerably high productivity (6–9 kgpropene kgcat−1 h−1). Moreover, with this catalyst, propene productivity only slightly decreased as a function of propane conversion, indicating that propene combustion toward COx occurs more slowly in comparison to other catalysts exhibiting high propene productivities. A detailed kinetic analysis of the 4V/13Ti/SBA-15 catalyst revealed that high vanadia and titania dispersions are required for high propene productivity.
Co-reporter:Riny Y. Parapat, Oey H. I. Saputra, Anton P. Ang, Michael Schwarze and Reinhard Schomäcker  
RSC Advances 2014 vol. 4(Issue 92) pp:50955-50963
Publication Date(Web):02 Oct 2014
DOI:10.1039/C4RA10736E
It is well known that the activities of supported metal catalysts are strongly dependent upon the size, shape and dispersion of the nanoparticles on the support material. There are several techniques which can be implemented in order to produce such catalysts, e.g. wet impregnation, however the deposition of nanoparticles (NPs) on the support material without agglomeration still proves a challenge. This is particularly significant when attempting to maintain the size and shape of the particles during the deposition process. We have introduced a new method to deposit metal NPs, namely thermo-destabilization of microemulsions (please see J. Mater. Chem., 2012, 22, 11605–11614 and Nanoscale, 2013, 5, 796–805), in which the NPs are formed prior the deposition process. This method is an ingenious approach to control the dispersion of NPs on the support material and depositing NPs evenly with a narrow size distribution. In this paper we expound the important role of the surface charges of NPs and the support material, as indicated by zeta potentials, on the metal dispersion, and how they affect the catalytic activity. We also investigate the influence of other parameters such as the pore size and the pre-calcination of the support on the catalytic activities of the resulting supported metal catalysts.
Co-reporter:Xiao Xie, Torsten Otremba, Patrick Littlewood, Reinhard Schomäcker, and Arne Thomas
ACS Catalysis 2013 Volume 3(Issue 2) pp:224
Publication Date(Web):December 26, 2012
DOI:10.1021/cs3003963
Silica supported nanoparticles of nickel manganese oxide, Ni0.2Mn0.8O, were prepared in a one-pot approach, combining co-precipitation and sol–gel chemistry. This approach enables the preparation of small ternary oxide crystallites evenly dispersed on porous silica. The resulting materials were used as catalyst for dry reforming of methane (DRM), and show a much higher activity as the reference bulk material prepared from conventional co-precipitation. Notably, the catalyst shows a remarkable activity even at low temperatures for DRM, thus nearly reaching thermodynamic equilibrium at 500 °C.Keywords: activation; carbon dioxide; dry reforming; heterogeneous catalysis; metal oxide catalyst; methane
Co-reporter:Herbert Over and Reinhard Schomäcker
ACS Catalysis 2013 Volume 3(Issue 5) pp:1034
Publication Date(Web):April 4, 2013
DOI:10.1021/cs300735e
The Deacon process is a sustainable way to recover chlorine from HCl by its oxidation with molecular oxygen. Deacon catalysts need to fulfill both selection criteria: high activity and high stability. In this Review, we introduce and discuss simple descriptors for assessing activity and stability of catalyst materials. A promising descriptor for ranking the experimental activities of Deacon catalysts and other oxidation catalysts in the form of oxides represents the dissociation energy of molecular oxygen as introduced by Studt et al. (ChemCatChem.2010, 2, 98). The resulting volcano plot allows for identifying promising catalyst materials for the Deacon process, such as exemplified with La2O3.Keywords: activity; BEP relation; Deacon process; HCl oxidation; heterogeneous catalysis; stability; volcano curve
Co-reporter:Riny Y. Parapat, Muliany Wijaya, Michael Schwarze, Sören Selve, Marc Willinger and Reinhard Schomäcker  
Nanoscale 2013 vol. 5(Issue 2) pp:796-805
Publication Date(Web):27 Nov 2012
DOI:10.1039/C2NR32122J
We recently introduced a new method to synthesize an active and stable Pt catalyst, namely thermo-destabilization of microemulsions (see R. Y. Parapat, V. Parwoto, M. Schwarze, B. Zhang, D. S. Su and R. Schomäcker, J. Mater. Chem., 2012, 22 (23), 11605–11614). We are able to produce Pt nanocrystals with a small size (2.5 nm) of an isotropic structure i.e. truncated octahedral and deposit them well on support materials. Although we have obtained good results, the performance of the catalyst still needed to be improved and optimized. We followed the strategy to retain the small size but change the shape to an anisotropic structure of Pt nanocrystals which produces more active sites by means of a weaker reducing agent. We found that our catalysts are more active than those we reported before and even show the potential to be applied in a challenging reaction such as hydrogenation of levulinic acid.
Co-reporter:Henriette Nowothnick, Anke Rost, Tobias Hamerla, Reinhard Schomäcker, Christian Müller and Dieter Vogt  
Catalysis Science & Technology 2013 vol. 3(Issue 3) pp:600-605
Publication Date(Web):07 Nov 2012
DOI:10.1039/C2CY20629C
The Rh-catalyzed aqueous biphasic hydroformylation with the bidentate ligand SulfoXantPhos was investigated for different phase transfer agents (PTA). As such, polymer latices and microemulsions formed by non-ionic surfactants were used. In general, a higher PTA concentration enhances the reaction progress. The feasibility of catalyst recycling by simple phase separation is shown in principle. The Rh losses are low in the surfactant system and promising for a technical approach.
Co-reporter:Dipl.-Chem. Tobias Hamerla;Dipl.-Chem. Anke Rost;Dipl.-Ing. Yasemin Kasaka ;Dr. Reinhard Schomäcker
ChemCatChem 2013 Volume 5( Issue 7) pp:1854-1862
Publication Date(Web):
DOI:10.1002/cctc.201200744

Abstract

A hydrophilic metal–ligand complex formed from the precursor [dicarbonyl(acetylacetonato)rhodium(I)] {[Rh(acac)(CO)2]} and the bidentate ligand [2,7-bis(SO3Na)-4,5-bis(diphenylphosphino)-9,9-dimethylxanthene] (SulfoXantPhos), was found to be a suitable candidate as a catalyst complex for the hydroformylation of 1-dodecene in multiphase systems formulated from water, 1-dodecene, and a nonionic surfactant. To improve the solubilization of the olefin in the aqueous phase, surfactants were added. The multiphase system acted as a tunable solvent, through which not only the interfacial area was increased during the reaction but also the phase separation behavior could be manipulated through temperature changes, thus allowing an easy separation of the expensive rhodium complex from the organic phase after the reaction. The influence of different process parameters such as the type of surfactant, type of ligand, and the metal/ligand ratio was investigated and discussed. Also the influence of the phase state on the reaction was determined. Under optimized reaction conditions, turnover frequencies of >300 h−1 and selectivities of 98:2 towards the linear product could be achieved.

Co-reporter:Riny Y. Parapat, Veronica Parwoto, Michael Schwarze, Bingsen Zhang, Dang Sheng Su and Reinhard Schomäcker  
Journal of Materials Chemistry A 2012 vol. 22(Issue 23) pp:11605-11614
Publication Date(Web):04 May 2012
DOI:10.1039/C2JM15468D
A new technique to deposit nanoparticles synthesized in reverse micellar microemulsions onto support material without agglomeration is named thermal destabilization of microemulsion. The multifaceted Pt crystals, mostly truncated octahedra, were produced inside reverse micelles with an average size of 2.5 nm and a narrow size distribution. After deposition, the Pt crystals were found to be well dispersed on the support with an average size of 2.5 nm. After testing with hydrogenation of α-methyl styrene, the produced Pt-catalyst showed higher activity (6 times higher) and stability than commercial ones. The advantages of this synthesis route of nanoparticles include simple operation, and the ease of controlling the size and shape of nanoparticles without using capping agents.
Co-reporter:Jonas Dimroth;Uwe Schedler;Juliane Keilitz;Rainer Haag;Reinhard Schomäcker
Advanced Synthesis & Catalysis 2011 Volume 353( Issue 8) pp:1335-1344
Publication Date(Web):
DOI:10.1002/adsc.201000955

Abstract

Heterogenization is a powerful approach for the generation of easily recyclable catalysts. In this study, a modified tethered rhodium(III)- p-toluenesulfonyl-1,2-diphenylethylenediamine (Rh-TsDPEN) complex immobilized on polymeric supports was applied to kinetic and up-scaling experiments on the asymmetric transfer hydrogenation of acetophenone in water. Study of the catalyst has helped in understanding some aspects of its operating mode. The results indicate that, in the investigated range, a simple second-order model describes the enantioselective conversion of acetophenone to phenylethanol. Optimal reaction conditions were determined, and particularly the solution pH was found to play a decisive role for the activity and reusability of the catalyst. The good performance under optimized conditions emphasizes the practical usefulness of this recyclable catalytic system for environmentally benign asymmetric transfer hydrogenation processes.

Co-reporter: Reinhard Schomäcker;Dr. Michael Schwarze;Dr. Henriette Nowothnick;Anke Rost ;Tobias Hamerla
Chemie Ingenieur Technik 2011 Volume 83( Issue 9) pp:1343-1355
Publication Date(Web):
DOI:10.1002/cite.201100042

Abstract

In dieser Übersicht wird ein Konzept für die reaktionstechnische Nutzung von wässrigen Tensidlösungen und Wasser/Tensid/Lösungsmittel-Gemischen als Reaktionsmedien für katalytische Reaktionen vorgestellt. Dabei werden drei Beispiele beschrieben, für die ein Reaktionsmedium formuliert werden konnte, das sowohl optimale Bedingungen für den Ablauf der Reaktionen bietet als auch eine effiziente Rückgewinnung des Katalysators ermöglicht.

In this review a concept is introduced for the application of micellar solutions and microemulsions in chemical reaction engineering. For three examples it is shown how to formulate a reaction medium which offers optimal conditions for the reaction as well as for the catalyst recycling.

Co-reporter:Henriette Nowothnick;Jochanan Blum;Dr. Reinhard Schomäcker
Angewandte Chemie 2011 Volume 123( Issue 8) pp:1959-1962
Publication Date(Web):
DOI:10.1002/ange.201005263
Co-reporter:Henriette Nowothnick;Jochanan Blum;Dr. Reinhard Schomäcker
Angewandte Chemie International Edition 2011 Volume 50( Issue 8) pp:1918-1921
Publication Date(Web):
DOI:10.1002/anie.201005263
Co-reporter:Kirsten Langfeld;René Marschner;Dr. Benjamin Frank;Dr. Reinhard Schomäcker
ChemCatChem 2011 Volume 3( Issue 8) pp:1354-1358
Publication Date(Web):
DOI:10.1002/cctc.201100033

Abstract

A facile and rapid preparation method for a wide variety of medium surface area perovskite-type catalysts on the laboratory scale is presented. The cellulose templating method allows for catalysts with high phase purity, even at the relatively low calcination temperatures. Among the versatile compositions of perovskites based on the SrCoOx system, straightforward modifications could be performed to optimize the catalytic performance in the oxidation of CH4. Substitutions in both the A and B positions in the ABO3 lattice can remarkably affect the catalytic activity. Compared to other preparation methods, the cellulose templating method is a rapid process and the catalytic performances obtained with SrCoOx and LaCoOx are at least as good as with materials prepared by conventional methods.

Co-reporter:Kirsten Langfeld;Evgenii V. Kondratenko;Oliver Görke
Catalysis Letters 2011 Volume 141( Issue 6) pp:772-778
Publication Date(Web):2011 June
DOI:10.1007/s10562-011-0607-1
Nanostructured perovskite-type SrCoOx catalysts were prepared using a w/o-microemulsion as a soft template. Conventional co-precipitation and citric acid sol–gel were used as reference methods with regard to surface and bulk physico-chemical properties as well as catalytic performance in methane oxidation. The solids were characterised by XRD, SEM, TEM, EDX, N2-physisorption, TG-DTA-MS, ICP-OES, and H2-TPR techniques. The phase transformation temperature of the microemulsion-templated perovskites is by 150 K lower than that in the conventionally prepared ones. Therefore, this material is characterized by smaller crystallite sizes and higher surface areas. As result, it shows a higher activity in oxidative coupling of methane as compared to sol–gel and co-precipitated catalysts. The properties of the catalysts are weakly influenced by changing the specific synthesis parameters of the microemulsions.
Co-reporter:S. Arndt;U. Simon;S. Heitz;A. Berthold;B. Beck;O. Görke
Topics in Catalysis 2011 Volume 54( Issue 16-18) pp:
Publication Date(Web):2011 November
DOI:10.1007/s11244-011-9749-z
Li-doped MgO was prepared on different preparative routes and with different loadings. The catalytic activity was found to decay for all catalysts for 40 h time on stream. A detailed structural analysis of 0.5 wt% Li-doped MgO showed heavy losses of Li, reduced surface area and grain growth. A correlation between these factors and the deactivation could not be found. The reaction temperature and the flow rate were found to be the main deactivation parameters.
Co-reporter:Juan S. Milano-Brusco;Jamal Touitou
Journal of Surfactants and Detergents 2011 Volume 14( Issue 1) pp:103-111
Publication Date(Web):2011 January
DOI:10.1007/s11743-010-1204-9
Microemulsion systems with the nonionic surfactant p-tert-octylphenoxy polyethoxyethanol (OP9.5EO), the anionic surfactant dioctyl sulfosuccinate sodium salt (DOSS) and the narrow range nonionic surfactant alkyl polyethylene glycol ether (C10EO5) were used as solvent systems in the catalytic hydrogenation of dimethyl itaconate (DMI) catalysed by the water soluble catalyst complex Rh-TPPTS in order to achieve product isolation and catalyst recycling. The DOSS systems, which are more sensitive to the substrate and catalyst addition allowed for the hydrogenation to proceed with an initial hydrogenation rate about three times higher than with the nonionic surfactants, when the surfactant concentration was 15 wt%. Systems with 3 wt% surfactant were used in order to accomplish catalyst recycling. With a biphasic DOSS mixture a turnover number (TON) of 1,200 mol of DMI hydrogenated per mol of catalyst (Rh) was obtained in 3 consecutive runs. A three-phase system for the OP9.5EO mixture allowed the catalyst to be recycled 3 times and a TON of 1,500 in 4 runs was obtained. A TON of 800 in 2 runs was obtained using a three-phase C10EO5 mixture.
Co-reporter:Jonas Dimroth;Juliane Keilitz;Uwe Schedler;Reinhard Schomäcker;Rainer Haag
Advanced Synthesis & Catalysis 2010 Volume 352( Issue 14-15) pp:2497-2506
Publication Date(Web):
DOI:10.1002/adsc.201000340

Abstract

Catalyst immobilization through covalent attachment onto a support is one strategy to provide recyclable systems. Here, soluble and surface-functionalized solid polymers were used as supports for a modified tethered rhodium(III)-p-toluenesulfonyl-1,2-diphenylethylenediamine [Rh(III)-TsDPEN] complex. The supported catalysts were applied to the asymmetric transfer hydrogenation of phenyl ketones in aqueous solution of sodium formate. High ee values (up to 99%) and good activities were achieved. It was discovered that the solid polymer-supported catalyst could be recycled at least four times without a significant decrease of the activity when a mixture of sodium formate and formic acid was used as the hydrogen source. This catalytic system provides a promising approach towards an ecologically and economically rational production of enantioenriched building blocks.

Co-reporter:Juan S. Milano-Brusco, Henriette Nowothnick, Michael Schwarze and Reinhard Schomäcker
Industrial & Engineering Chemistry Research 2010 Volume 49(Issue 3) pp:1098-1104
Publication Date(Web):July 31, 2009
DOI:10.1021/ie900753t
The potential of surfactant based reaction media was studied with different homogeneous catalytic reactions. Micellar systems with the surfactants (p-tert-octylphenoxy) polyethoxyethanol (Triton X-100) and dodecyl sulfate sodium salt were used as reaction media for the enantioselective catalytic hydrogenation of dimethyl itaconate (DMI) with the Rh catalyst complexed with the chiral ligand (2S,4S)-1-tert-butoxycarbonyl-4-diphenylphosphino-2-(diphenylphosphinometyl)-pyrrolidine (BPPM) at 30 °C and 1.1 bar, obtaining an enantiomeric excess (ee) of up to 69%. After complete hydrogenation was achieved, micellar enhanced ultrafiltration (MEUF) was used to recycle the catalyst achieving up to 95% retention. A microemulsion system stabilized with the surfactant Triton X-100 was used as alternative reaction media for the hydrogenation of DMI with a Rh catalyst complexed with the water-soluble tris(3-sulfophenyl)phosphine trisodium salt (TPPTS) at 50 °C and 1.1 bar. With the Triton X-100 system, phase separation by temperature induced separation allowed for up to four repetitive batches of DMI hydrogenations, resulting in a TON of 1530. Suzuki coupling for the synthesis of 4′-methyl-2-biphenylcarbonitrile proceeded faster in a narrow range alkylpolyglycol ether (Novel 8 = Novel 1216CO-8 Ethoxylate) three-phase system than in an dioctyl sulfosuccinate sodium salt (AOT) two-phase system, demonstrating the retarding effect of the salinization on the reaction rate.
Co-reporter:Juan Milano-Brusco, Sylvain Prévost, Dersy Lugo, Michael Gradzielski and Reinhard Schomäcker  
New Journal of Chemistry 2009 vol. 33(Issue 8) pp:1726-1735
Publication Date(Web):02 Jun 2009
DOI:10.1039/B905063A
The structural dimensions of two different microemulsions were extracted and correlated with the catalytic hydrogenation of dimethyl itaconate (DMI) performed in such media using the water-soluble catalyst complex Rh–TPPTS. The commercial, polyoxyethylene-based non-ionic surfactants Igepal CA-520 and Triton X-100 were used to obtain two different types of microemulsions with cyclohexane and water; pentanol as a cosurfactant was added to the Triton system. Dynamic light scattering (DLS) and small angle neutron scattering (SANS) measurements were used to determine the characteristic sizes of the Igepal and Triton microemulsions, respectively, showing a linear dependence between the initial hydrogenation rate of DMI and the radius of the micelles. The initial hydrogenation rate of DMI in bulk water is exceeded in both microemulsions. Indications of deformation of the originally spherical Triton X-100 reverse micelles upon addition of the water-soluble catalyst complex Rh–TPPTS were found.
Co-reporter:Juan S. Milano-Brusco;Reinhard Schomäcker
Catalysis Letters 2009 Volume 133( Issue 3-4) pp:
Publication Date(Web):2009 December
DOI:10.1007/s10562-009-0187-5
The effect of the P/Rh ratio and the surfactant concentration on the partial hydrogenation of sunflower oil in Triton X-100 microemulsion systems with the water-soluble catalyst complex Rh-TPPTS has been studied. An unusual hindering effect of the surfactant on the production of elaidic acid and stearic acid as the oil is hydrogenated was observed. When increasing the concentration of Triton X-100 in the reaction medium from 3 to 15 wt%, the content of elaidic acid and stearic acid were lowered 21 and 34%, respectively. The maximum content of oleic acid was attained when the concentration of Triton X-100 was 15 wt%, obtaining a high content of 51.8% of oleic acid. When the ligand/metal ratio was higher, the reaction was slower but more selective to oleic acid. The Rh-TPPTS catalyst could be recycled up to 3 times after hydrogenation of sunflower oil by extracting the oil phase of a three-phase microemulsion system, observing a continuous deactivation of the catalyst.
Co-reporter:Arne Dinse, Sonia Khennache, Benjamin Frank, Christian Hess, Rita Herbert, Sabine Wrabetz, Robert Schlögl, Reinhard Schomäcker
Journal of Molecular Catalysis A: Chemical 2009 Volume 307(1–2) pp:43-50
Publication Date(Web):15 July 2009
DOI:10.1016/j.molcata.2009.03.008
Silica (SBA-15) supported vanadium oxide was used for a kinetic study of the oxidative dehydrogenation of propane in a fixed bed reactor. Prior to this study, spectroscopic characterization using a variety of analytic techniques such as FTIR-, Raman-, DR UV–vis- and X-ray photoelectron spectroscopy revealed the absence of bulk vanadia and a high dispersion of active surface sites for the investigated catalyst. The kinetic data evaluation was based on a first order rate law. Calorimetric measurements were used to determine the heat of adsorption of propane on the catalyst.The data indicate that the primary combustion of propane is negligible. Reaction orders of one for propane dehydrogenation and propene combustion indicate their participation in the respective rate-determining step. The zero reaction order determined for the catalyst reoxidation reveals participation of lattice oxygen in this reaction step. Higher activation energies of propane dehydrogenation as compared to propene combustion indicate the participation of the weaker allylic C–H bond of propene in the rate-determining step of the propene combustion. This results in higher propene selectivities at elevated temperatures. Kinetic parameters, including apparent and intrinsic activation energies and the equilibrium constant of propane adsorption allowed a comparison with theoretical predictions and show good agreement.A kinetic strudy was implemented to elucidate the reaction mechanism of oxidative dehydrogenation of propane (ODP) on a structurally well characterized silica (SBA-15) supported vanadia catalyst. Furthermore, calorimetric measurements were used to investigate the adsorption behaviour of propane on the catalyst surface. Reaction orders indicate a participation of propane and propene in the respective rate-determining steps of the particular partial reaction and a fast reoxidation of the reduced catalytic site. The results of the kinetic modelling and the adsorption experiments were used to calculate the real activation energies of the reaction.
Co-reporter:Juan S. Milano-Brusco, Michael Schwarze, M’hamed Djennad, Henriette Nowothnick and Reinhard Schomäcker
Industrial & Engineering Chemistry Research 2008 Volume 47(Issue 20) pp:7586
Publication Date(Web):September 13, 2008
DOI:10.1021/ie800190g
The kinetics of the catalytic hydrogenation of dimethyl itaconate (DMI) was studied in a biphasic cyclohexane−water system and in a [Triton X-100/1-pentanol]/cyclohexane/water microemulsion, in both cases using the water-soluble catalyst complex Rh−TPPTS. The reaction was carried out at a pressure of 1.1 bar and in the temperature range 298−308 K. A typical profile of a zero-order reaction was observed in the case of the biphasic system. Against that the reaction order for DMI changed to 1 in a microemulsion. A rate law based on an Osborn−Wilkinson-like kinetics was used to describe the experimental results which were governed by the irreversible attack of free DMI at the rhodium complex. The activation energy of the rate-determining step is 53 kJ mol−1 and is similar in both systems.
Co-reporter:Gregor Schinkel, Immo Garrn, Benjamin Frank, Ulrich Gernert, Helmut Schubert, Reinhard Schomäcker
Materials Chemistry and Physics 2008 Volume 111(2–3) pp:570-577
Publication Date(Web):15 October 2008
DOI:10.1016/j.matchemphys.2008.05.032
The engineering aspects of the preparation of nanostructured alumina ceramic precursors by alcoholate hydrolysis using microemulsions as reaction media are investigated here. The precipitate was subjected to several treatment steps. Although the properties of the primary precipitated powders are independent of the chemical or reaction engineering parameters of the precipitation procedure, the structure of treated powders and sintered, dense ceramics strongly depends on thermal and mechanical handling like crystallization or grinding of the alumina ceramic precursor. Strong differences are manifested in relative densities and sintering kinetics and can be observed by SEM analysis.
Co-reporter:R. Schomäcker Dr.;B. Frank Dr.;H. Soerijanto Dr.;M. Lerch Dr.;R. Schlögl Dr.
Chemie Ingenieur Technik 2008 Volume 80( Issue 9) pp:
Publication Date(Web):
DOI:10.1002/cite.200750763

No abstract is available for this article.

Co-reporter:O. Schwarz, D. Habel, O. Ovsitser, E.V. Kondratenko, C. Hess, R. Schomäcker, H. Schubert
Journal of Molecular Catalysis A: Chemical 2008 Volume 293(1–2) pp:45-52
Publication Date(Web):1 October 2008
DOI:10.1016/j.molcata.2008.07.009
Two preparation methods (wet saturation impregnation with vanadyl acetylacetonate and ball-milling of γ-Al2O3 with crystalline V2O5) were applied to produce two sets of VOx/γ-Al2O3 catalysts with increasing vanadium loadings. Materials from both sets were characterized by XRD, SEM, Raman, TPR and UV/vis-DRS (UV/vis diffuse reflectance spectroscopy) to elucidate the influence of the preparation method on the morphology of VOx species and on their behavior in the oxidative dehydrogenation of propane (ODP). Edge energies from UV/vis-DRS experiments were correlated with activity and selectivity data; the lower the edge energy, the lower catalytic activity and the higher propene selectivity. Both preparation methods result in materials with comparable physico-chemical and catalytic properties although very different precursors were used. Especially the calcination step during catalyst preparation seems to transform the different precursor molecules to dispersed VOx species by an equilibration process on the support material surface.Two preparation methods (wet saturation impregnation and ball-milling) were applied to produce VOx/γ-Al2O3 materials with comparable physico-chemical and catalytic properties although very different precursors were used. The calcination step during catalyst preparation was found to be essential for dispersing VOx species on the support material surface. A correlation between edge energies derived from UV/vis-DRS experiments and catalytic performance was established.
Co-reporter:Arne Dinse, Benjamin Frank, Christian Hess, Daniela Habel, Reinhard Schomäcker
Journal of Molecular Catalysis A: Chemical 2008 Volume 289(1–2) pp:28-37
Publication Date(Web):17 June 2008
DOI:10.1016/j.molcata.2008.04.007
The influence of the support material of low-loaded (<2 V nm−2) vanadia catalysts on selectivities, activation energies and turn over frequencies in the oxidative dehydrogenation of propane and the combustion of propene was investigated. CeO2, TiO2, Al2O3, ZrO2 and SiO2 supported catalysts were prepared by saturation wetness impregnation in toluene. Characterization with temperature-programmed reduction and Raman spectroscopy revealed a high dispersion of surface vanadia species for all investigated catalysts. The impact of heat and mass transfer limitations on the catalytic performance has been thoroughly excluded. Selectivities towards propene as well as activation energies strongly depend on the support material. For all catalysts, propene selectivity increases with temperature. Deconvolution of the reaction network of oxidative dehydrogenation of propane (ODP) into decoupled reactions of different reactants for at least three of the catalysts is not possible, because of a significant impact of the oxidation state of the catalyst on the reaction. Except for the CeO2 supported catalyst, the contribution of the bare support material on the activity can be neglected.This study investigates the influence of the support material on the catalytic performance of supported vanadia catalysts (surface density of vanadium <2 V nm−2) on the oxidative dehydrogenation of propane (ODP). It is shown that the respective support material strongly influences the selectivity towards the desirable product propene as well as the catalytic activity. The highest selectivity catalyst is achieved with an alumina supported vanadia catalyst.
Co-reporter:O. Schwarz;A. Dinse;R. Schomäcker ;G. Schäfer Dr.
Chemie Ingenieur Technik 2007 Volume 79(Issue 9) pp:
Publication Date(Web):18 SEP 2007
DOI:10.1002/cite.200750061
Co-reporter:R. Schomäcker Dr.;M. Schwarze Dipl.-Chem.;J. Milano Dipl.-Ing.;S. Jost Dipl.-Ing.
Chemie Ingenieur Technik 2007 Volume 79(Issue 9) pp:
Publication Date(Web):18 SEP 2007
DOI:10.1002/cite.200750183
Co-reporter:Devender S. Negi;Tobias Kimmel
Journal of the American Oil Chemists' Society 2007 Volume 84( Issue 1) pp:91-96
Publication Date(Web):2007 January
DOI:10.1007/s11746-006-1010-8
The glycerolysis of methyl ester was investigated in flow reactors. This reaction represents a liquid two-phase reaction with changing reaction rates in a batch reactor. A semi-empirical model tested earlier with batch reactor data was used to simulate different continuous processes for this reaction. Among the processes simulated, a single continuous-flow stirred tank reactor (CSTR) without recycling was considered most appropriate for experimental implementation, although simulations showed that a faster reaction rate is possible with the application of a CSTR followed by a tubular reactor with certain associated residence times. The CSTR simulations were verified experimentally. A good agreement was found between the experimental data and simulation results.
Co-reporter:Devender S. Negi;Felix Sobotka
Journal of the American Oil Chemists' Society 2007 Volume 84( Issue 1) pp:83-90
Publication Date(Web):2007 January
DOI:10.1007/s11746-006-1009-1
The present work focused on the glycerolysis of fatty acid methyl esters. The aim was to develop and test a kinetic model that could be used to reliably simulate different process alternatives for this reaction. A prerequisite was the identification and characterization of the factors that affect the reaction kinetics. Experiments were carried out in a batch reactor with and without forced removal of methanol, which is one of the reaction products. Concentrations of all components in the two-phase system were measured. It was found that the methanol concentration has a strong effect on the reaction rate and equilibrium conversion. Near-complete conversions were obtained by stripping methanol with an inert gas. The glycerol concentration in the ester phase was found to increase as the reaction proceeds, which also accelerates the reaction. Effects of mass transfer on the reaction rate were not found to control the reaction rate under well-agitated conditions. A semi-empirical model was used to simulate the reaction. The results from the semi-empirical model show good agreement with experimental results.
Co-reporter:B. Frank;A. Yildiz;D. Habel;H. Schubert;R. Schomäcker
Chemical Engineering & Technology 2006 Volume 29(Issue 4) pp:
Publication Date(Web):23 MAR 2006
DOI:10.1002/ceat.200500380

A commercially available niobia hydrate, which is an industrial intermediate in the production of pure niobia, was prepared, characterized, and tested as a solid acid catalyst. The gas phase esterification of acetic acid with ethanol was used as a simple model reaction for the determination of the acidity and the catalytic activity. The kinetic evaluation of the experiments includes an estimation of mass transport limitation as well as a mechanistic study.

Co-reporter:M. Schwarze Dipl.-Chem.;R. Schomäcker Dr.
Chemie Ingenieur Technik 2006 Volume 78(Issue 7) pp:
Publication Date(Web):3 JUL 2006
DOI:10.1002/cite.200600038

Bei der Herstellung von Feinchemikalien und Pharmazeutika werden vermehrt homogene Katalysatoren eingesetzt. Für einen wirtschaftlich nutzbaren Prozess ist es erforderlich, den Katalysator mehrmals wieder zu verwenden. Im Anschluss an eine stereoselektive Hydrierreaktion ist es prinzipiell möglich, zur Katalysatorrückgewinnung die „Micellar Enhanced Ultrafiltration” (MEUF) einzusetzen. Für Membranen mit einem Cutoff von 10 kDa und kleiner zeigen sich Katalysatorrückhalte > 98 %. Bei der Katalysatorrückgewinnung im technischen Maßstab stellt sich die Frage, welcher Rückhalt erreicht werden muss, um das Produkt wirtschaftlich zu erzeugen.

Co-reporter:B. Frank Dipl.-Ing.;A. Yildiz Dipl.-Ing.;R. Schomäcker Dr. rer. nat.;D. Habel Dipl.-Ing.;H. Schubert Dr. rer. nat.
Chemie Ingenieur Technik 2006 Volume 78(Issue 1-2) pp:
Publication Date(Web):24 JAN 2006
DOI:10.1002/cite.200500150

Ein kommerziell erhältliches Nioboxid-Hydrat, das bei der Darstellung von Nioboxid als Zwischenprodukt anfällt, wird auf seine Eignung als Feststoffsäure-Katalysator untersucht. Die Veresterung von Essigsäure mit Ethanol in der Gasphase dient für die Beurteilung der Aktivität als einfache Modellreaktion. Die kinetische Auswertung der Versuche umfasst sowohl eine mechanistische Studie als auch Abschätzungen über Stofftransporthemmungen.

Co-reporter:R. Schomäcker;A. Schmidt;B. Frank;R. Haidar;A. Seidel-Morgenstern
Chemie Ingenieur Technik 2005 Volume 77(Issue 5) pp:
Publication Date(Web):3 MAY 2005
DOI:10.1002/cite.200500043

Durch den Einsatz von Membranen und Membranreaktoren in der Katalyse bieten sich verschiedene Möglichkeiten, den Umsatz, die Selektivität und die Raum-Zeit-Ausbeute von katalytischen Prozessen zu steigern. Am Beispiel von porösen Polymermembranen, in die Palladium-Nanopartikel eingebettet sind, wird das Konzept der Anwendung von katalytisch aktiven Membranen für Hydrierreaktionen vorgestellt.

Co-reporter:Bernhard Orlich;Reinhard Schomäcker
Chemical Engineering & Technology 1999 Volume 22(Issue 9) pp:
Publication Date(Web):31 AUG 1999
DOI:10.1002/(SICI)1521-4125(199909)22:9<753::AID-CEAT753>3.0.CO;2-Q
Co-reporter:Dipl.-Ing. Bernhard Orlich; Dr. Reinhard Schomäcker
Chemie Ingenieur Technik 1999 Volume 71(Issue 1-2) pp:
Publication Date(Web):3 FEB 2004
DOI:10.1002/cite.330710128
Co-reporter:S. Arndt, B. Uysal, A. Berthold, T. Otrebma, ... R. Schomäcker
Journal of Natural Gas Chemistry (September 2012) Volume 21(Issue 5) pp:581-594
Publication Date(Web):1 September 2012
DOI:10.1016/S1003-9953(11)60407-6
ZnO could be a suitable catalyst for the oxidative conversion of CH4, C2H6 and C3H8. However, the main drawback is its thermal instability. Therefore, ZnO supported on ZrO2, TiO2, γ-Al2O3 and SiO2 was investigated for the oxidative dehydrogenation of propane and ethane, and the oxidative coupling of methane. The stability of the supported ZnO is partially improved, but ZnO reacts with the support material, forming new compounds (Zn-zirconates, -titanates, -aluminates and -silicates), which already occurs below reaction temperature. This might also be the case for many other heterogeneous catalysts.
Co-reporter:Benjamin Beck, Manuel Harth, Neil G. Hamilton, Carlos Carrero, John J. Uhlrich, Annette Trunschke, Shamil Shaikhutdinov, Helmut Schubert, Hans-Joachim Freund, Robert Schlögl, Joachim Sauer, Reinhard Schomäcker
Journal of Catalysis (December 2012) Volume 296() pp:120-131
Publication Date(Web):1 December 2012
DOI:10.1016/j.jcat.2012.09.008
The influence of the support material of vanadia catalysts on the reaction rate, activation energies, and defect formation enthalpies was investigated for the oxidative dehydrogenation of ethanol and propane. Characterization by infrared absorption–reflection spectroscopy (IRAS), Raman and UV–vis spectroscopy verifies a high dispersion of vanadia for powder and thin-film model catalysts. The support effect of ceria, alumina, titania, and zirconia is reflected in activation energy, oxidative dehydrogenation (ODH) rate, and temperature-programmed reductions (TPR) for both catalyst systems, ethanol and propane. Impendence spectroscopy and density functional theory (DFT) calculations were used to determine the defect formation enthalpy of the vanadyl oxygen double bond, providing the scaling parameter for a Bell–Evans–Polanyi relationship. On the basis of a Mars–van-Krevelen mechanism, an energy profile for the oxidative dehydrogenation is proposed.Graphical abstractThe influence of the support material of vanadia catalysts on reaction rate, activation energies, and defect formation enthalpies of the vanadyl oxygen bond was investigated for the oxidative dehydrogenation of ethanol and propane. A relationship following a Bell–Evans–Polanyi principle was found between defect formation enthalpy and activation energy.Download high-res image (68KB)Download full-size imageHighlights► Support effect is found in powder as in thin-film model catalysts. ► Support effect is proven by density functional theory (DFT) calculations. ► Linear correlation found between apparent activation energies of ethanol and propane. ► Activation energies follow Bell–Evans–Polanyi (BEP) principle with defect formation enthalpies.
Co-reporter:M. Yildiz, Y. Aksu, U. Simon, T. Otremba, K. Kailasam, C. Göbel, F. Girgsdies, O. Görke, F. Rosowski, A. Thomas, R. Schomäcker, S. Arndt
Applied Catalysis A: General (5 September 2016) Volume 525() pp:168-179
Publication Date(Web):5 September 2016
DOI:10.1016/j.apcata.2016.06.034
Co-reporter:Benjamin Frank, Arne Dinse, Olga Ovsitser, Evgueni V. Kondratenko, Reinhard Schomäcker
Applied Catalysis A: General (30 April 2007) Volume 323() pp:66-76
Publication Date(Web):30 April 2007
DOI:10.1016/j.apcata.2007.02.006
Co-reporter:S. Arndt, T. Otremba, U. Simon, M. Yildiz, H. Schubert, R. Schomäcker
Applied Catalysis A: General (28 May 2012) Volumes 425–426() pp:53-61
Publication Date(Web):28 May 2012
DOI:10.1016/j.apcata.2012.02.046
Co-reporter:M.’hamed. Djennad, Djafer Benachour, Reinhard. Schomäcker
Procedia Engineering (2012) Volume 33() pp:70-77
Publication Date(Web):1 January 2012
DOI:10.1016/j.proeng.2012.01.1178
The partition coefficients of different solutes as Itaconic acid (IA), dimethyl itaconate (DMI), diethyl itaconate (DEI) and dibuthyl itaconate (DBI) between water and micelles of Triton X-100 are determined by the two methods of separation namely Cross Flow Filtration and Dead-End Filtration by using a membrane that rejects the micelles and lets passing the molecules of solute. Partition coefficient of the solute between the aqueous phase and micelle aggregate was determined by titration and HPLC methods. The results obtained are discussed in our researcher's group and compared to others made with theoretical data reported from simulation. The effect of the different concentrations of solutes and transmembrane pressures have been investigated using a commercial membrane Nadir C005 (MWCO = 5 kDa).
Co-reporter:B. Frank, F.C. Jentoft, H. Soerijanto, J. Kröhnert, R. Schlögl, R. Schomäcker
Journal of Catalysis (15 February 2007) Volume 246(Issue 1) pp:177-192
Publication Date(Web):15 February 2007
DOI:10.1016/j.jcat.2006.11.031
Steam reforming of methanol (SRM) was investigated over copper-containing catalysts supported on four different oxides and mixed oxides: Cu/ZnO/Al2O3, Cu/ZrO2/CeO2, Cu/SiO2, and Cu/Cr2O3/Fe2O3. After observing slight differences in the way of catalyst aging and experimental exclusion of mass transport limitation effects, a detailed kinetic study was carried out at 493 K. The dependence of the reaction rate on the molar ratio of methanol and water was determined, as was the influence of addition of inert nitrogen and the main reaction products hydrogen and carbon dioxide to the reactant mixture. Although there were remarkable differences in the catalytic activity of the samples, the main mechanistic steps reflected in the rate law were similar for all catalysts. The reaction rate is determined mainly by the methanol partial pressure, whereas water is not involved in the rate-determining step, except over Cu/Cr2O3/Fe2O3, where several differences in the chemistry were observed. Hydrogen and carbon dioxide were found to inhibit the reaction. These results were confirmed by a DRIFT study at 493 K using an equimolar reactant mixture and an excess of 4:1 of water and methanol, respectively. The same surface species could be identified on each catalyst, but neither kinetic modeling nor the DRIFT spectra could clearly indicate whether the reaction pathway occurs via a dioxomethylene species or a methyl formate species as intermediate. Similar activation energies of SRM confirm the assumption that the surface chemistry of SRM over copper-based systems is independent of the catalyst support material.
Co-reporter:Benjamin Frank, Rémy Fortrie, Christian Hess, Robert Schlögl, Reinhard Schomäcker
Applied Catalysis A: General (1 February 2009) Volume 353(Issue 2) pp:288-295
Publication Date(Web):1 February 2009
DOI:10.1016/j.apcata.2008.11.002
Co-reporter:Carlos Carrero, Markus Kauer, Arne Dinse, Till Wolfram, Neil Hamilton, Annette Trunschke, Robert Schlögl and Reinhard Schomäcker
Catalysis Science & Technology (2011-Present) 2014 - vol. 4(Issue 3) pp:NaN794-794
Publication Date(Web):2013/12/13
DOI:10.1039/C3CY00625E
Grafted VxOy catalysts for oxidative dehydrogenation of propane (ODP) have been studied due to their potential high performance and as model catalysts in the past. We report on a positive synergetic effect capable of considerably enhancing the propene productivities above reported performances. The most productive catalysts were found at metal loadings (V + Ti) close to the monolayer coverage. The 4V/13Ti/SBA-15 catalyst presented a considerably high productivity (6–9 kgpropene kgcat−1 h−1). Moreover, with this catalyst, propene productivity only slightly decreased as a function of propane conversion, indicating that propene combustion toward COx occurs more slowly in comparison to other catalysts exhibiting high propene productivities. A detailed kinetic analysis of the 4V/13Ti/SBA-15 catalyst revealed that high vanadia and titania dispersions are required for high propene productivity.
Co-reporter:Henriette Nowothnick, Anke Rost, Tobias Hamerla, Reinhard Schomäcker, Christian Müller and Dieter Vogt
Catalysis Science & Technology (2011-Present) 2013 - vol. 3(Issue 3) pp:NaN605-605
Publication Date(Web):2012/11/07
DOI:10.1039/C2CY20629C
The Rh-catalyzed aqueous biphasic hydroformylation with the bidentate ligand SulfoXantPhos was investigated for different phase transfer agents (PTA). As such, polymer latices and microemulsions formed by non-ionic surfactants were used. In general, a higher PTA concentration enhances the reaction progress. The feasibility of catalyst recycling by simple phase separation is shown in principle. The Rh losses are low in the surfactant system and promising for a technical approach.
Co-reporter:M. Yildiz, Y. Aksu, U. Simon, K. Kailasam, O. Goerke, F. Rosowski, R. Schomäcker, A. Thomas and S. Arndt
Chemical Communications 2014 - vol. 50(Issue 92) pp:NaN14442-14442
Publication Date(Web):2014/10/10
DOI:10.1039/C4CC06561A
The oxidative coupling of methane is a highly promising reaction for its direct conversion. Silica supported MnxOy–Na2WO4 is a suitable catalyst for this reaction. In this study, a variety of different SiO2 materials have been tested as supports. Surprisingly, the application of ordered mesoporous silicas, here exemplarily shown for SBA-15 as support materials, greatly enhances the catalytic performance. The CH4 conversion increased two fold and also the C2 selectivity is strongly increased.
Co-reporter:Riny Y. Parapat, Veronica Parwoto, Michael Schwarze, Bingsen Zhang, Dang Sheng Su and Reinhard Schomäcker
Journal of Materials Chemistry A 2012 - vol. 22(Issue 23) pp:NaN11614-11614
Publication Date(Web):2012/05/04
DOI:10.1039/C2JM15468D
A new technique to deposit nanoparticles synthesized in reverse micellar microemulsions onto support material without agglomeration is named thermal destabilization of microemulsion. The multifaceted Pt crystals, mostly truncated octahedra, were produced inside reverse micelles with an average size of 2.5 nm and a narrow size distribution. After deposition, the Pt crystals were found to be well dispersed on the support with an average size of 2.5 nm. After testing with hydrogenation of α-methyl styrene, the produced Pt-catalyst showed higher activity (6 times higher) and stability than commercial ones. The advantages of this synthesis route of nanoparticles include simple operation, and the ease of controlling the size and shape of nanoparticles without using capping agents.
Sodium 2-(dicyclohexylphosphino)-2',6'-dimethoxybiphenyl-3'-sulfonate
catASium(R) MN(R)Rh, 2,3-Bis[(2R,5R)-2,5-dimethylphospholanyl]malein-N-methylimide(1,5-cyclooctadiene)rhodium(I) tetrafluoroborate
Iron lanthanum strontium oxide
Dibenzo[d,f][1,3,2]dioxaphosphepin,6,6'-[[3,3'-bis(1,1-dimethylethyl)-5,5'-dimethoxy[1,1'-biphenyl]-2,2'-diyl]bis(oxy)]bis-