ZrO2-Based Alternatives to Conventional Propane Dehydrogenation Catalysts: Active Sites, Design, and Performance

2015 ◽  
Vol 54 (52) ◽  
pp. 15880-15883 ◽  
Author(s):  
Tatyana Otroshchenko ◽  
Sergey Sokolov ◽  
Mariana Stoyanova ◽  
Vita A. Kondratenko ◽  
Uwe Rodemerck ◽  
...  
2021 ◽  
Vol 504 ◽  
pp. 111466
Author(s):  
Yu-Ling Shan ◽  
Wen-Ting Zhao ◽  
Shi-Lei Zhao ◽  
Xiu-Xin Wang ◽  
Huai-Lu Sun ◽  
...  

1997 ◽  
Vol 62 (2) ◽  
pp. 347-354 ◽  
Author(s):  
Milan Hájek

Microwave heating was applied in homogeneous and in heterogeneous reactions and the results were compared from the point of view of activation of chemical reactions. Reactions including the addition of halo compounds to alkenes catalyzed by copper and ruthenium complexes in different solvents and NaY zeolite catalyzed alkylation of secondary amine in the absence of solvent were studied as model reactions to compare possibilities of microwave activation of reactants and catalysts. Rate enhancement of over one order of magnitude in homogeneous reactions was caused mainly by thermal dielectric heating effect which resulted from the effective coupling of microwaves to polar solvents. Activation of reactants and catalysts was very low if any. In heterogeneously catalyzed alkylation reactions highly efficient activation of zeolite catalyst was recorded. The results indicated that the best reaction conditions were in experiments when both activation of catalyst and performance of reaction were carried out under microwave conditions. Rate enhancement was most probably caused by "hot spots" or by "selective heating" of active sites. In both homogeneous and heterogeneous reactions non-thermal activation (specific effect) was excluded.


Owing to recent developments there is now a prodigality of crystalline inorganic solids capable of catalysing the chemical conversions of numerous gaseous molecules, especially hydrocarbons. Very many of these new catalysts are microporous and microcrystalline, and have their accessible active sites distributed uniformly throughout their bulk. They are, therefore, amenable to investigation by essentially all of the premier experimental and computational tools of solid-state physics and solid-state chemistry. The deployment of these tools has yielded fresh insights into the mechanisms of catalytic action and also suggested new strategies, some of which have already been tested, for the design of specially tailored selective catalysts. The benefits of multi-pronged approaches to the investigation of the reactivity of catalysts, made possible by the combined use of intense X -ray sources (both laboratory-based and synchrotron radiation) and supercomputers, are illustrated by specific reference to zeolitic solids that contain cages and channels of molecular dimension. Such crystalline solids, either in their highly acidic or metal-ionexchanged forms, are of great practical value on an industrial scale. They are also ideally suited for in situ exploration of the subtle structural changes that accompany, or are responsible for, the activation and deactivation of catalysts. Ways of optimizing the performance of catalysts, including the possible construction of ‘teabag’ analogues, and of coping computationally with their properties and performance so as to deepen our understanding of their mode of operation are outlined with reference to both the zeolites and the ever-widening range of solid oxides crystallizing with pyrochlore and perovskite structures.


2015 ◽  
Vol 327 ◽  
pp. 86-95 ◽  
Author(s):  
Esther Bailón-García ◽  
Francisco Carrasco-Marín ◽  
Agustín F. Pérez-Cadenas ◽  
Francisco J. Maldonado-Hódar

2016 ◽  
Vol 708 ◽  
pp. 94-97 ◽  
Author(s):  
Noor Asmawati Mohd Zabidi ◽  
Sara Tasfy ◽  
Maizatul Shima Shaharun

Hydrogenation of CO2 provides an alternative route for methanol production and attractive option for CO2 utilization. The present work investigates the synthesis of Cu-based catalyst on mesoporous silica (SBA-15) and promotion of the Cu-based catalyst with niobium (Nb). The addition of Nb promoter enhanced the reducibility and dispersion of the active sites as well as increased the BET and Cu surface areas. The performance of the synthesized catalyst in the hydrogenation of CO2 was evaluated in a fixed-bed microreactor at 523K, 22.5bar and H2/CO2 of 3. The CO2 conversion using the Cu/ZnO/SBA-15 catalyst was 14.2 % and increased to 17.1% on the Nb-promoted catalyst. The yield of methanol obtained using the un-promoted Cu-based catalyst was 51.4 g/h.gcat and it increased to 143 g/h.gcat over the Nb-promoted catalyst.


Author(s):  
Wei Zhang ◽  
Hongfei Ma ◽  
Haizhi Wang ◽  
Jiawei Jiang ◽  
Zhi-Jun Sui ◽  
...  

An experiment-obtained volcano-type curve is observed on propane dehydrogenation over a group of atomically dispersed Pt catalysts supported on various supports. The oxide state of Ptδ+ active sites via charge-transfer...


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