Catalysis with Ordered Porous Materials

A special issue of Catalysts (ISSN 2073-4344). This special issue belongs to the section "Catalytic Materials".

Deadline for manuscript submissions: closed (30 June 2021) | Viewed by 10855

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Guest Editor
UMR 7197, Laboratoire de Réactivité de Surface (LRS), Centre National de la Recherche Scientifique, Sorbonne Université, 75252 Paris, France
Interests: utilization of porous materials for the design of selective and stable catalysts; valorization of alkenes, CO2, and biomass; supported homogeneous catalysts (organocatalysts, metal complexes, polyoxometalates or even enzymes); supported heterogeneous catalysts (zero-valent metal/metal oxide colloids)
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Special Issue Information

Dear Colleagues,

Heterogeneous catalysis is in essence based on the exploitation of the interactions of molecules with solid surfaces. Therefore, one of the most important challenges for the development of efficient heterogeneous catalysts is to make available as many active sites as possible to the reagents while allowing an efficient release of the products. This is one of the reasons why the design of high-performance heterogeneous catalysts is linked in particular to the progress obtained in the development of porous materials properly dimensioned and stable enough under the conditions of the targeted reactions. Zeolites, because of their relatively high stability and the progress made in their synthesis over many years, are widely represented in industrial heterogeneous catalysis processes today. Such materials are intrinsically active in acid-base catalysis and can be used as metals supports, thus covering a wide range of applications in catalysis. Moreover, the pioneering work carried out on these materials has paved the way for the exploitation of porous supports, in general, with the aim also of influencing the selectivity of catalytic processes, in particular by means of confinement effects.

Since then, the variety of organized porous supports available has increased considerably with, in the 1990s, the development of oxides, carbons, and polymers with structured mesopores, in the 2000s, the development of metal organic frameworks (MOF) and even more recently, covalent organic frameworks (COF). This has allowed different ways of adapting the porosity scales and organization while controlling the surface properties as closely as possible, to the point of establishing connections between homogeneous and heterogeneous catalysis. The hierarchization of porosity, based, for example, on the combination of micropores and mesopores, has also opened up interesting prospects for a more extensive exploitation of zeolites in applications, which were previously handicapped by diffusion limitations. Additionally, the incorporation of macropores and implementation in the forms of monoliths instead of powders are very up-to-date topics, particularly for the development of processes operating continuously in the liquid phase.

The objective of this Special Issue is to emphasize the contribution(s) that porous materials can provide to the performance of heterogeneous catalysts. We are interested in the investigation of structure–property relationships. Main fields of application targeted here are energy, fine chemistry, and pollution control processes. The active phases can be simple metals, metal complexes, nanoparticles, etc. and even enzymes or combinations opening up new fields of application. Thus, several examples of studies claiming an improvement in the stability of enzymes once they are grafted onto porous supports have been published, leaving the possibility of developing tandem heterogeneous catalysis involving biocatalysts and supported chemical catalysts. Other interesting issues which are not exhaustive concern photocatalysis or the possibilities of intensification by exploiting pre-concentration phenomena by adsorption of reagents within porous catalysts.

Prof. Dr. Franck Launay
Guest Editor

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Keywords

  • heterogeneous catalysis
  • porous materials
  • zeolites
  • pore sizes
  • stability
  • microporous
  • mesoporous
  • macroporous
  • metal
  • enzymes
  • adsorption
  • selectivity
  • confinement
  • oxides
  • carbons
  • polymers
  • hierarchical porosity
  • tandem catalysis
  • Metal-organic frameworks (MOF)
  • Covalent-organic frameworks (COF)
  • monoliths
  • photocatalysis

Published Papers (4 papers)

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Research

15 pages, 16002 KiB  
Article
Magnesium Impregnated on NaX Zeolite Synthesized from Cogon Grass Silica for Fast Production of Fructose via Microwave-Assisted Catalytic Glucose Isomerization
by Sittichai Kulawong, Saran Youngjan, Pongtanawat Khemthong, Narong Chanlek, Jatuporn Wittayakun and Nattawut Osakoo
Catalysts 2021, 11(8), 981; https://0-doi-org.brum.beds.ac.uk/10.3390/catal11080981 - 17 Aug 2021
Viewed by 2255
Abstract
Fructose is a crucial intermediate in the production of several chemical platforms. Fructose is mainly produced from glucose isomerization either through immobilized enzymes or heterogeneous catalysts using a conventional heating source, and this is time-consuming. Thus, this work discloses a fast production of [...] Read more.
Fructose is a crucial intermediate in the production of several chemical platforms. Fructose is mainly produced from glucose isomerization either through immobilized enzymes or heterogeneous catalysts using a conventional heating source, and this is time-consuming. Thus, this work discloses a fast production of fructose via microwave-assisted catalytic glucose isomerization using Mg catalysts supported on NaX zeolite from cogon grass silica. The catalysts were prepared by the impregnation of magnesium nitrate solution and subsequently transformed into MgO on NaX by calcination. The effect of 3, 6 and 9 wt.% Mg content on NaX on the performance of glucose isomerized to fructose was tested at 90 °C for 15 min. The best catalyst was selected for studying the effect of reaction times of 5, 15, 30 and 60 min. Results from X-ray diffraction (XRD), N2 sorption and CO2 temperature-programmed desorption (CO2-TPD) suggested that crystallinity, surface area and micropore volume decrease but basicity increases with Mg content. The X-ray photoelectron spectroscopy (XPS) result confirmed the presence of mixed phases of MgO and Mg2CO3 in all catalysts. The glucose conversion enhanced with the Mg loading but the fructose yield gave the highest value with Mg of 6 wt.%, probably due to the tuning of high active sites and surface area. The greatest fructose selectivity and yield (71.9% and 25.8%) were obtained within 15 min by microwave-assisted catalytic reaction, shorter than the reported value in the literature, indicating a suitable reaction time. Mg (6 wt.%)/NaX catalyst preserves the original catalytic performance up to three cycles, indicating that it is a promising catalyst for fructose production. Full article
(This article belongs to the Special Issue Catalysis with Ordered Porous Materials)
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13 pages, 3469 KiB  
Article
Cu-IM-5 as the Catalyst for Selective Catalytic Reduction of NOx with NH3: Role of Cu Species and Reaction Mechanism
by Guangying Fu, Junwen Chen, Yuqian Liang, Rui Li, Xiaobo Yang and Jiuxing Jiang
Catalysts 2021, 11(2), 221; https://0-doi-org.brum.beds.ac.uk/10.3390/catal11020221 - 07 Feb 2021
Cited by 10 | Viewed by 2319
Abstract
The role of Cu species in Cu ion-exchanged IM-5 zeolite (Cu-IM-5) regarding the performance in selective catalytic reduction (SCR) of NOx with NH3 (NH3-SCR) and the reaction mechanism was studied. Based on H2 temperature-programmed reduction (H2-TPR) [...] Read more.
The role of Cu species in Cu ion-exchanged IM-5 zeolite (Cu-IM-5) regarding the performance in selective catalytic reduction (SCR) of NOx with NH3 (NH3-SCR) and the reaction mechanism was studied. Based on H2 temperature-programmed reduction (H2-TPR) and electron paramagnetic resonance (EPR) results, Cu–O–Cu and isolated Cu species are suggested as main Cu species existing in Cu-IM-5 and are active for SCR reaction. Cu–O–Cu species show a good NH3-SCR activity at temperatures below 250 °C, whereas their NH3 oxidation activity at higher temperatures hinders the SCR performance. At low temperatures, NH4NO3 and NH4NO2 are key reaction intermediates. In situ diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS) suggests a mixed Eley–Rideal (E–R) and Langmuir–Hinshelwood (L–H) mechanism over Cu-IM-5 at low temperatures. Full article
(This article belongs to the Special Issue Catalysis with Ordered Porous Materials)
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16 pages, 6934 KiB  
Article
On the Support Effect and the Cr Promotion of Co Based Catalysts for the Acetic Acid Steam Reforming
by Marta Cortese, Concetta Ruocco, Vincenzo Palma, Pedro J. Megía, Alicia Carrero and José A. Calles
Catalysts 2021, 11(1), 133; https://0-doi-org.brum.beds.ac.uk/10.3390/catal11010133 - 18 Jan 2021
Cited by 7 | Viewed by 2181
Abstract
This work focuses on the support effect of the performances of Co based catalysts for acetic acid steam reforming. SBA-15, a well ordered hexagonal mesoporous silica structure, and CeO2 have been selected as the supports, with the impact of chromium addition also [...] Read more.
This work focuses on the support effect of the performances of Co based catalysts for acetic acid steam reforming. SBA-15, a well ordered hexagonal mesoporous silica structure, and CeO2 have been selected as the supports, with the impact of chromium addition also being investigated. Better acetic acid steam reforming performances have been recorded for CeO2 compared to SBA-15 supported catalysts and, in particular, the 7Co/CeO2 catalyst showed the highest values of acetic acid conversions with enhanced H2 yields below 480 °C, in comparison to the other investigated catalytic formulations. In addition, more pronounced coke depositions and acetone concentrations have been obtained with CeO2 supported catalysts, due to the tendency of ceria to catalyse the ketonization reaction. Chromium addition to Co/SBA-15 catalysts led to an enhancement in the activity towards acetic acid steam reforming, while on CeO2 supported catalysts no improvement in the catalysts’ activity was observed. However, on both SBA-15 and CeO2 supported catalysts, Cr addition reduced the amount of coke deposited on the catalysts surface. Full article
(This article belongs to the Special Issue Catalysis with Ordered Porous Materials)
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16 pages, 4051 KiB  
Article
A Comprehensive Study of Coke Deposits on a Pt-Sn/SBA-16 Catalyst during the Dehydrogenation of Propane
by Jose P. Ruelas-Leyva, Luis F. Maldonado-Garcia, Alfonso Talavera-Lopez, Iván A. Santos-López, Lorenzo A. Picos-Corrales, Carlos E. Santolalla-Vargas, Sergio A. Gómez Torres and Gustavo A. Fuentes
Catalysts 2021, 11(1), 128; https://0-doi-org.brum.beds.ac.uk/10.3390/catal11010128 - 16 Jan 2021
Cited by 12 | Viewed by 3248
Abstract
Catalytic propane dehydrogenation is an attractive method to produce propylene while avoiding the issues of its traditional synthesis via naphtha steam cracking of naphtha. In this contribution, a series of Pt-Sn/SBA-16 catalysts were synthesized and evaluated for this purpose. Bimetallic Pt-Sn catalysts were [...] Read more.
Catalytic propane dehydrogenation is an attractive method to produce propylene while avoiding the issues of its traditional synthesis via naphtha steam cracking of naphtha. In this contribution, a series of Pt-Sn/SBA-16 catalysts were synthesized and evaluated for this purpose. Bimetallic Pt-Sn catalysts were more active than catalysts containing only Pt. The catalyst with the best performance was assessed at different reaction times of 0, 60, 180, and 300 min. The evolution of coke deposits was also studied. Thermogravimetric analysis demonstrated the presence of two types of coke on the catalyst surface at low and high temperature, respectively. Raman results showed an increased coke’s crystal size from 60 to 180 min on stream, and from 180 to 300 min under reaction, Raman suggested a reduction in the crystal size of coke. Also transmission electron microscopy confirmed a more evident agglomeration of metallic particles with reaction times higher than 180 min. These results are consistent with the phenomena called “coke migration” and the cause is often explained by coke movement near the particle to the support; it can also be explained due to sintering of the metallic particle, which we propose as a more suitable explanation. Full article
(This article belongs to the Special Issue Catalysis with Ordered Porous Materials)
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