2021
DOI: 10.3389/fmats.2020.617432
|View full text |Cite
|
Sign up to set email alerts
|

Carbon-Based Materials as Catalyst Supports for Fischer–Tropsch Synthesis: A Review

Abstract: The use of carbon-based materials as catalyst supports for Fischer–Tropsch synthesis (FTS) is thoroughly reviewed. The main factors to consider when using a carbonaceous catalyst support for FTS are first discussed. Then, the most relevant and recent literature on the topic from the last 2 decades is reviewed, classifying the different examples according to the carbon structure and shape. Some aspects such as the carbon textural properties, carbon support modification (functionalization and doping), catalyst p… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

2
18
0

Year Published

2021
2021
2024
2024

Publication Types

Select...
8
1

Relationship

1
8

Authors

Journals

citations
Cited by 37 publications
(21 citation statements)
references
References 152 publications
2
18
0
Order By: Relevance
“…While the calculated ratio could be interpreted as an active site ratio (vide supra), the strict meaning of this model-parameter corresponds to the average relative probability of each CO-dissociation mechanism to occur, as calculated by our SEMK model, over the investigated range of operating conditions. Also, during operation, the catalyst surface is inherently dynamic [127][128][129] and the step-to-terrace site ratio therefore depends on the employed operating conditions. Such a detailed analysis of the catalyst surface and active sites is beyond the scope of the presented work.…”
Section: Abundance Of the Different Sitesmentioning
confidence: 99%
“…While the calculated ratio could be interpreted as an active site ratio (vide supra), the strict meaning of this model-parameter corresponds to the average relative probability of each CO-dissociation mechanism to occur, as calculated by our SEMK model, over the investigated range of operating conditions. Also, during operation, the catalyst surface is inherently dynamic [127][128][129] and the step-to-terrace site ratio therefore depends on the employed operating conditions. Such a detailed analysis of the catalyst surface and active sites is beyond the scope of the presented work.…”
Section: Abundance Of the Different Sitesmentioning
confidence: 99%
“…Because of the high thermal conductivity and at high carbonization temperature, the carbon support yields lower interactions with the metal active sites. 97,98 Table 6 shows that the utilization of carbon supports gives high selectivity to hydrocarbons above 60%, with the exception of sibunit. The templated synthesis method to obtain mesoporous carbon exhibits the highest conversion (50.6%) and selectivity to hydrocarbons (91.8%), with 44.5% C 5+ .…”
Section: Types Of Support For Ft Reactivitymentioning
confidence: 99%
“…In CO FT conversion with a silica-supported catalyst, the dominant phase of iron is Fe 2 O 3 , while on a carbon-supported catalyst, the magnetite/maghemite phase is predominant, hence, with a higher carburization to active phase Fe 2 C 5 . Because of the high thermal conductivity and at high carbonization temperature, the carbon support yields lower interactions with the metal active sites. , …”
Section: Types Of Support For Ft Reactivitymentioning
confidence: 99%
“…The defects and doping components are responsible for the strength of the bond between the metal and the substrate, and can also provide specific electronic effects [69]. It is often noted that the presence of a large volume of micropores in the substrate can reduce the activity of the supported catalyst due to mass transfer limitations [70,71].…”
Section: Which Properties Of the Support Determine The Activity Of The Catalyst?mentioning
confidence: 99%