2019
DOI: 10.1016/j.cej.2019.04.102
|View full text |Cite
|
Sign up to set email alerts
|

Study on the redox characteristics of CaCo based oxygen carrier for Chemical Looping Combustion

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
2

Citation Types

0
6
0

Year Published

2021
2021
2024
2024

Publication Types

Select...
7

Relationship

0
7

Authors

Journals

citations
Cited by 13 publications
(6 citation statements)
references
References 31 publications
0
6
0
Order By: Relevance
“…The reason behind this was that the activation energy for reduction was larger than that for oxidation. 55 It may also be that, since the oxidation was exothermic while the reduction was endothermic, local heating during oxidation may have accelerated its reaction as compared to reduction. For the 15NA-ULT OC (see Figure 6), the times required to oxidize and reduce the ULT sample were only 2 and 3 min, respectively.…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…The reason behind this was that the activation energy for reduction was larger than that for oxidation. 55 It may also be that, since the oxidation was exothermic while the reduction was endothermic, local heating during oxidation may have accelerated its reaction as compared to reduction. For the 15NA-ULT OC (see Figure 6), the times required to oxidize and reduce the ULT sample were only 2 and 3 min, respectively.…”
Section: Resultsmentioning
confidence: 99%
“…The curves for the oxidation were also steeper than those of the reduction reaction. The reason behind this was that the activation energy for reduction was larger than that for oxidation . It may also be that, since the oxidation was exothermic while the reduction was endothermic, local heating during oxidation may have accelerated its reaction as compared to reduction.…”
Section: Resultsmentioning
confidence: 99%
“…For reduction and oxidation processes, 5% CH 4 /N 2 (for 3 min) and air (for 10 min) were used at a flow rate of 80 mL/min, respectively. However, the temperature of the furnace is kept constant at 800 °C. , Between methane and air, nitrogen gas was purged for 3 min to avoid mixing between methane and air. The OTC of OCs during 10 redox cycles was calculated using eq . OTC = m ox m red m ox where, m ox is the mass of fully oxidized OC and m red is the mass of fully reduced OC.…”
Section: Methodsmentioning
confidence: 99%
“…However, the temperature of the furnace is kept constant at 800 °C. 14 , 18 Between methane and air, nitrogen gas was purged for 3 min to avoid mixing between methane and air. The OTC of OCs during 10 redox cycles was calculated using eq 1 .…”
Section: Methodsmentioning
confidence: 99%
“…3,26 Also as a VIII group element, metallic Co has already been demonstrated active for glycerol steam reforming, 10,20,27 and the chemical-looping hydrogen combustion was realized over Ca 3 Co 2 O 6 . 28 On this basis, we proposed that CCO is a potential OC that can be applied for a CLMC process. and CO 2 in the off-gas were monitored by a GC9790 online gas chromatograph (GC) equipped with a TDX-1 packed column, a methanator, a TCD, and a flame ionization detector.…”
mentioning
confidence: 99%