2022
DOI: 10.1016/j.fuel.2022.125470
|View full text |Cite
|
Sign up to set email alerts
|

Hydrogenation of CO2 to light olefins on ZZ/MnSAPO-34@Si-2: Effect of silicalite-2 seeds on the acidity and catalytic activity

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

0
4
0

Year Published

2022
2022
2024
2024

Publication Types

Select...
5

Relationship

0
5

Authors

Journals

citations
Cited by 5 publications
(5 citation statements)
references
References 39 publications
0
4
0
Order By: Relevance
“…Specifically, a high selectivity of C 5+ hydrocarbons (91.9 %) was achieved via RWGS‐FTS route over a Fe−Zn‐Zr@HZSM‐5 catalyst, where the optimum zeolite BAS density and shell thickness was achieved by utilizing this strategy, exhibiting its potential to steer product selectivity [138] . Furthermore, the core‐shell concept has recently garnered attention for CO 2 hydrogenation as multiple studies observed an increased olefin selectivity, compared to the physical mixing of the same catalyst components [102,112–113] . However, several unanswered questions persist, such as, what is the interaction between the active sites, and whether there can be any effect of ion migration in such arrangements.…”
Section: Discussionmentioning
confidence: 99%
See 1 more Smart Citation
“…Specifically, a high selectivity of C 5+ hydrocarbons (91.9 %) was achieved via RWGS‐FTS route over a Fe−Zn‐Zr@HZSM‐5 catalyst, where the optimum zeolite BAS density and shell thickness was achieved by utilizing this strategy, exhibiting its potential to steer product selectivity [138] . Furthermore, the core‐shell concept has recently garnered attention for CO 2 hydrogenation as multiple studies observed an increased olefin selectivity, compared to the physical mixing of the same catalyst components [102,112–113] . However, several unanswered questions persist, such as, what is the interaction between the active sites, and whether there can be any effect of ion migration in such arrangements.…”
Section: Discussionmentioning
confidence: 99%
“…[138] Furthermore, the core-shell concept has recently garnered attention for CO 2 hydrogenation as multiple studies observed an increased olefin selectivity, compared to the physical mixing of the same catalyst components. [102,[112][113] However, several unanswered questions persist, such as, what is the interaction between the active sites, and whether there can be any effect of ion migration in such arrangements. A thorough exploration of these factors can pave the way for the development of an optimal catalyst for the efficient and selective hydrogenation of CO 2 .…”
Section: Core-shell Catalystmentioning
confidence: 99%
“…Therefore, from the conventional Fischer-Tropsch reaction, it is possible to access catalytic systems that could be tested in modified Fischer-Tropsch processes capable of using CO 2 as a raw material to access light olefins (C2-C4) widely used in different fields such as the synthesis of polymers and pharmaceutical intermediates. However, the chain length distributions are given by the Anderson-Flory (ASF) distribution, which limit the C2-C4 range to less than 58% [427]. Finally, it is possible to integrate waste CO 2 in synthesis using Fe-based Fischer-Tropsch with green H 2 as well as olefin oligomerization, thereby increasing the production of value-added liquid hydrocarbons [428].…”
Section: Modified Fischer-tropsch Synthesis Routementioning
confidence: 99%
“…[17] The thermal catalysis of CO 2 can be divided into CO 2 -COhydrocarbons and CO 2 -methanol-hydrocarbons according to different reaction principles. [18,19] Methanol as an intermediate product is more selective for the product, but the CO 2 utilization is generally lower. [20] CO 2 -CO-hydrocarbons is also a modified Fischer-Tropsch process, typically having higher CO 2 utilization and easier access to long-chain hydrocarbons.…”
Section: Introductionmentioning
confidence: 99%
“…The thermal catalysis of CO 2 can be divided into CO 2 ‐CO‐hydrocarbons and CO 2 ‐methanol‐hydrocarbons according to different reaction principles [18,19] . Methanol as an intermediate product is more selective for the product, but the CO 2 utilization is generally lower [20] .…”
Section: Introductionmentioning
confidence: 99%