2003
DOI: 10.1023/b:catl.0000004105.58023.b6
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Stability of MCM-41-Supported CoMo Hydrotreating Catalysts

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Cited by 17 publications
(4 citation statements)
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“…A material with a high specific surface and a sizable pore diameter together with proper acidic functions has been the main goal of many researchers in this area. To date, the discovery of MCM-41 mesoporous silica has proven to be the material of choice. However, their poor thermal stability has posed serious limitations on their practical applications. , New mesoporous silica-type materials have been developed in recent years, intending to optimize the synthesis methods to obtain mesoporous supports similar to MCM-41. So far, it seems that SBA-15 is the best candidate to replace MCM-41, so long as one can minimize the limitations found when thermal and hydrothermal stability are considered but retain the advantages of the materials that they intend to replace .…”
Section: Introductionmentioning
confidence: 99%
“…A material with a high specific surface and a sizable pore diameter together with proper acidic functions has been the main goal of many researchers in this area. To date, the discovery of MCM-41 mesoporous silica has proven to be the material of choice. However, their poor thermal stability has posed serious limitations on their practical applications. , New mesoporous silica-type materials have been developed in recent years, intending to optimize the synthesis methods to obtain mesoporous supports similar to MCM-41. So far, it seems that SBA-15 is the best candidate to replace MCM-41, so long as one can minimize the limitations found when thermal and hydrothermal stability are considered but retain the advantages of the materials that they intend to replace .…”
Section: Introductionmentioning
confidence: 99%
“…It was found that zirconium improves hydrogenation activities of the samples. However, the MCM-41 and HMS type materials have poor stability [28,29] and relatively small pores (about 20-35 Å diameter), which can be easily blocked by HDS active phases [27]. These disadvantages represent a serious limitation to the practical applications of MCM-41 or HMS-based formulations.…”
Section: Introductionmentioning
confidence: 99%
“…One of the most important topics is the design of HDS catalytic materials . Alumina is considered as the typical support material in the industrial processes due to its low cost, good properties, and ease of synthesis. , However, there are also some drawbacks, mainly related to the presence of undesired metal–support interactions, which severely restricts the formation of NiMoS-II active phases. , To overcome the aforementioned disadvantages of commercial support and realize the ultradeep HDS, different supports like MCM-41, , HMS, , KIT-6, , and SBA-15 , have been used in HDS reactions. However, these one- or two-dimensional supports cannot provide more space for reactant and product molecules to diffuse in and out .…”
Section: Introductionmentioning
confidence: 99%
“…19,20 However, there are also some drawbacks, mainly related to the presence of undesired metal−support interactions, which severely restricts the formation of NiMoS-II active phases. 21,22 To overcome the aforementioned disadvantages of commercial support and realize the ultradeep HDS, different supports like MCM-41, 23,24 HMS, 25,26 KIT-6, 27,28 and SBA-15 29,30 have been used in HDS reactions. However, these one-or two-dimensional supports cannot provide more space for reactant and product molecules to diffuse in and out.…”
Section: Introductionmentioning
confidence: 99%