Severity: Warning
Message: file_get_contents(https://...@pubfacts.com&api_key=b8daa3ad693db53b1410957c26c9a51b4908&a=1): Failed to open stream: HTTP request failed! HTTP/1.1 429 Too Many Requests
Filename: helpers/my_audit_helper.php
Line Number: 176
Backtrace:
File: /var/www/html/application/helpers/my_audit_helper.php
Line: 176
Function: file_get_contents
File: /var/www/html/application/helpers/my_audit_helper.php
Line: 250
Function: simplexml_load_file_from_url
File: /var/www/html/application/helpers/my_audit_helper.php
Line: 3122
Function: getPubMedXML
File: /var/www/html/application/controllers/Detail.php
Line: 575
Function: pubMedSearch_Global
File: /var/www/html/application/controllers/Detail.php
Line: 489
Function: pubMedGetRelatedKeyword
File: /var/www/html/index.php
Line: 316
Function: require_once
Transformations of oxygenates (CO, CO, HO, etc.) via MoC-based catalysts are facilitated by the high oxophilicity of the material; however, this can lead to the formation of oxycarbides and complicate the identification of the (most) active catalyst state and active sites. In this context, the two-dimensional (2D) MXene molybdenum carbide MoC ( are passivating surface groups) contains only surface Mo sites and is therefore a highly suitable model catalyst for structure-activity studies. Here, we report that the catalytic activity of MoC in Fischer-Tropsch (FT) synthesis increases with a decreasing coverage of surface passivating groups (mostly O*). The removal of species and its consequence on CO conversion is highlighted by the observation of a very pronounced activation of MoC (pretreated in H at 400 °C) under FT conditions. This activation process is ascribed to the reductive defunctionalization of groups reaching a catalyst state that is close to 2D-MoC (i.e., a material containing no passivating surface groups). Under steady-state FT conditions, 2D-MoC yields higher hydrocarbons (C alkanes) with 55% selectivity. Alkanes up to the kerosine range form, with value of α = 0.87, which is ca. twice higher than the α value reported for 3D-MoC catalysts. The steady-state productivity of 2D-MoC to C hydrocarbons is ca. 2 orders of magnitude higher relative to a reference β-ΜoC catalyst that shows no activation under identical FT conditions. The passivating groups of MoC can be reductively defunctionalized also by using a higher H pretreatment temperature of 500 °C. Yet, this approach leads to a removal of carbidic carbon (as methane), resulting in a 2D-MoC catalyst that converts CO to CH with 61% selectivity in preference to C hydrocarbons that are formed with only 2% selectivity. Density functional theory (DFT) results attribute the observed selectivity of 2D-MoC to C alkanes to a higher energy barrier for the hydrogenation of surface alkyl species relative to the energy barriers for C-C coupling. The removal of O* is the rate-determining step in the FT reaction over 2D-MoC, and O* is favorably removed in the form of CO relative to HO, consistent with the observation of a high CO selectivity (ca. 50%). The absence of other carbon oxygenates is explained by the energetic favoring of the direct over the hydrogen-assisted dissociative adsorption of CO.
Download full-text PDF |
Source |
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http://www.ncbi.nlm.nih.gov/pmc/articles/PMC10845113 | PMC |
http://dx.doi.org/10.1021/acscatal.3c03956 | DOI Listing |
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