2019
DOI: 10.1016/j.fuel.2019.01.018
|View full text |Cite
|
Sign up to set email alerts
|

Thermodynamics and kinetics analysis of Ca-looping for CO2 capture: Application of carbide slag

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

0
10
0

Year Published

2020
2020
2023
2023

Publication Types

Select...
8
1

Relationship

0
9

Authors

Journals

citations
Cited by 59 publications
(11 citation statements)
references
References 52 publications
0
10
0
Order By: Relevance
“…The rate constants of CO 2 capture with MgO·FeO x @NSC at different temperatures were compared (Figure b). The values of k were calculated to be 0.0799, 0.113, and 0.144 min –1 at temperatures of 50, 100, and 200 °C, respectively, indicating the effectiveness of the first-order reaction model for CO 2 adsorption with the MgO·FeO x @NSC material, thus implying that chemical sorption should be the rate-limiting step of the CO 2 capture process. , …”
Section: Results and Discussionmentioning
confidence: 99%
See 1 more Smart Citation
“…The rate constants of CO 2 capture with MgO·FeO x @NSC at different temperatures were compared (Figure b). The values of k were calculated to be 0.0799, 0.113, and 0.144 min –1 at temperatures of 50, 100, and 200 °C, respectively, indicating the effectiveness of the first-order reaction model for CO 2 adsorption with the MgO·FeO x @NSC material, thus implying that chemical sorption should be the rate-limiting step of the CO 2 capture process. , …”
Section: Results and Discussionmentioning
confidence: 99%
“…The values of k were calculated to be 0.0799, 0.113, and 0.144 min −1 at temperatures of 50, 100, and 200 °C, respectively, indicating the effectiveness of the firstorder reaction model for CO 2 adsorption with the MgO• FeO x @NSC material, thus implying that chemical sorption should be the rate-limiting step of the CO 2 capture process. 33,34 As for the equilibrium adsorption capacity of MgO•FeO x @ NSC, as shown in Figure 3a, the CO 2 equilibrium adsorption capacity quickly increased from 2.27 to 4.57 mol/kg with the temperature increasing from 50 to 100 °C. With the temperature further increasing to 200 °C, the CO 2 equilibrium adsorption capacity decreased to 2.81 mol/kg.…”
Section: Mg(oh)mentioning
confidence: 99%
“…The activation energy can be obtained by combining experimental data by both model fitting and model-free isoconversion rate methods, with values typically ranging from 100 to 230 kJ/mol. For powdered CaCO 3 calcination kinetics, reported models include the diffusion control model and the chemical reaction control model. Some research demonstrated that the CaCO 3 decomposition mechanism followed the diffusion control model (one-dimensional (1D) or two-dimensional (2D)). , Numerous investigations have confirmed the predominance of the chemical mechanism (phase boundary or nucleation and nuclear growth). Additionally, there are also some studies on the effect of CaCO 3 physicochemical features, heating rate, and CO 2 partial pressure on the chemical reaction mechanism. , …”
Section: Introductionmentioning
confidence: 99%
“…The composition of CS includes Ca(OH) 2 , CaCO 3 , and small amounts of MgO, SiO 2 , Al 2 O 3 , Fe 2 O 3 [47]. The annual output of CS is about 5:6 × 10 7 tons in China [48]. CS can be used as raw material to prepare cement binder or acid gas absorbent.…”
Section: Introductionmentioning
confidence: 99%