2020
DOI: 10.1016/j.apcatb.2020.119302
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Effect of copper on highly effective Fe-Mn based catalysts during production of light olefins via Fischer-Tropsch process with low CO2 emission

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Cited by 72 publications
(30 citation statements)
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“…To investigate the chemisorption behavior of the prepared sample, which is important to the synthesized β-SiC when it is used as catalyst support, 53 the CO 2 -temperature programmed desorption (CO 2 -TPD) experiment was performed. As shown in Figure 4c, two desorption peaks can be recognized.…”
Section: ■ Results and Discussionmentioning
confidence: 99%
“…To investigate the chemisorption behavior of the prepared sample, which is important to the synthesized β-SiC when it is used as catalyst support, 53 the CO 2 -temperature programmed desorption (CO 2 -TPD) experiment was performed. As shown in Figure 4c, two desorption peaks can be recognized.…”
Section: ■ Results and Discussionmentioning
confidence: 99%
“…Where, the manganese carbonate phase has been reported to be possibly formed during reaction for the intimate contact of MnO with CO 2 , leading to the detrimental catalytic behavior. [10] While, on the other hand the catalyst without Mn inclusion in Na-3Fe0.5Co shows the decrease of carbide peaks with the relative enhancement of Fe 3 O 4 Figure S6, resulting to the lower catalytic performance than that of Na- [17] 300 20 2 96.9 23.0 20.0 40.1 9.5 / Fe/CNF [41] 300 20 2 88.0 42.0 13.0 52.0 18.0 / FeBi/CNT [42] 350 [44] 320 20 1 85.0 48.0 22.7 39.4 29.7 / MnCr/HZ [45] 430 40 1 13 45.0 6.7 19.5 2.9 70.9 Fe 3 O 4 @MnO 2 /HZ [28] 320 [47] 350 40 1 18.3 49 1.5 16.9 27.9 53.6 FeMnKSiO 2 /HZ [48] 300 [49] 350 20 2 88.8 27.5 9.6 26.6 13.2 50.6 KFeMn/HZ [38] 320 [16] 310 3Fe2Mn0.5Co. Moreover, it can also be seen that C 5 + fraction has been escalated in liquid phase for both Na-3Fe2Mn2Co & Na-3Fe0.5Co catalyst that apparently indicating a higher fraction of liquid paraffins in C 5 + hydrocarbons being difficult to be aromatized on zeolite surface as compared to that of olefins in Na-3Fe2Mn0.5Co catalyst.…”
Section: Mechanistic Insights Of Bimetallic Ft Synthesis/aromatizatiomentioning
confidence: 97%
“…The addition of Mn as transition metal auxiliary in Na-3Fe 2 Mn catalyst, yielded majorly as Mn 3 O 4 phase with JCPDS 24-0734 at the diffraction peaks of 18.08°, 28.88°, 32.3°36.03°, 53.82°and 65.34°with some peaks of Fe 2 O 3 (Figure 1a, d) inferring that the dissolution of iron atom into the Mn 3 O 4 could impart an efficient interaction between Fe and Mn phase being attributed to the formation of solid solution as per our recent study. [17] It is well known that the specific difference in peak parameters of XRD pattern is the valuable indication for the doped structures possessing a lattice mismatch between the corresponding metal oxides due to different atomic radius of two different elements. [18] While, the effective inclusion of foreign elements into the lattice structure of host element may lead to the desired and expedient manipulation in electron density of the host element that could possibly enhance the generation of oxygen vacancies.…”
Section: Catalyst Characterization Of Calcined Samplesmentioning
confidence: 99%
“…Unfortunately, this pathway is a two-step process and energy intensive, where carbon monoxide (CO) must be formed through utilization of the water−gas shift reaction and then reacted with hydrogen (H 2 ) gas at high temperatures and pressures to get final usable products. 9,10 Therefore, there is an urgent need to revolutionize and update the energy industry, and this update could come from the electrochemical CO 2 RR to form value-added fuels and chemicals. The primary work that originally introduced CO 2 RR to the world was done by Hori in the 1980s, where he exhibited the capabilities of different pure metal catalysts to reduce CO 2 , which opened the door for large amounts of research to be conducted on CO 2 RR.…”
Section: Introductionmentioning
confidence: 99%
“…According to an assessment by the U.S. Energy Information Administration, unless the current energy structure is changed, CO 2 levels in the atmosphere will continue to increase. , On the industrial scale, currently the Fischer–Tropsch synthesis pathway is the main process of producing carbonaceous feedstock chemicals. Unfortunately, this pathway is a two-step process and energy intensive, where carbon monoxide (CO) must be formed through utilization of the water–gas shift reaction and then reacted with hydrogen (H 2 ) gas at high temperatures and pressures to get final usable products. , Therefore, there is an urgent need to revolutionize and update the energy industry, and this update could come from the electrochemical CO 2 RR to form value-added fuels and chemicals.…”
Section: Introductionmentioning
confidence: 99%