2009
DOI: 10.1134/s086986430904009x
|View full text |Cite
|
Sign up to set email alerts
|

Direct conversion of solid hydrocarbons in a molten carbonate fuel cell

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1
1

Citation Types

3
17
0

Year Published

2012
2012
2022
2022

Publication Types

Select...
6

Relationship

0
6

Authors

Journals

citations
Cited by 13 publications
(20 citation statements)
references
References 11 publications
3
17
0
Order By: Relevance
“…337,339 Interestingly, the main issue associated with the prolonged use of MCFCs is the degradation of the cell components instead of the decomposition of molten salt electrolyte. The reason is that the cell operating temperature is relatively high (typically between 600 o C to 850 o C due to the high melting temperature of carbonates) 340 when compared to that of hydroxide based fuel cells, 337,[341][342][343][344] which is problematic to the construction materials of the cell components. However, the eutectic carbonate salt mixture is adequately stable at the operating temperatures.…”
Section: Liquid Metal Batteriesmentioning
confidence: 99%
“…337,339 Interestingly, the main issue associated with the prolonged use of MCFCs is the degradation of the cell components instead of the decomposition of molten salt electrolyte. The reason is that the cell operating temperature is relatively high (typically between 600 o C to 850 o C due to the high melting temperature of carbonates) 340 when compared to that of hydroxide based fuel cells, 337,[341][342][343][344] which is problematic to the construction materials of the cell components. However, the eutectic carbonate salt mixture is adequately stable at the operating temperatures.…”
Section: Liquid Metal Batteriesmentioning
confidence: 99%
“…Activation energies tended to decrease (processes became more facile) as wt% H and volatile matter content increased. Enhanced reactivity of coals with higher wt% H [11] and the i n t e r n a t i o n a l j o u r n a l o f h y d r o g e n e n e r g y 4 0 ( 2 0 1 5 ) 1 9 4 5 e1 9 5 8 significance of volatile matter [29] have previously been reported for MCFC-type DCFCs ((LieK) 2 CO 3 , 700 C).…”
Section: Carbon Fuelmentioning
confidence: 88%
“…Bubble evolution due to carbonate decomposition at elevated temperature (600 C) has been studied by Kim et al (2014) [37]. Bubble formation at solid/molten carbonate reactive interfaces has been well illustrated by Chen et al [38], and the effects of bubble formation at anode reactive sites in a single chamber MCFC-type DCFC have been reported [11]. These single-chamber experiments consisted of a (38e62 mol % LieK) 2 CO 3 containing vessel where the carbon fuel was kept separate from the cathode by meshes, which also served as current collectors, and cathode gases (O 2 eCO 2 ) were introduced at 700e800 C [39].…”
Section: Reaction Mechanismmentioning
confidence: 96%
See 1 more Smart Citation
“…22 Among cannel coal, anthracite and graphite, cannel coal had the highest hydrogen content, therefore, the best maximum power density of the cell was obtained with this coal. Moisture is another parameter to be considered, and this has been plotted with the relationship of power output over a period of 24 hours in Figure 11c.…”
Section: Discussionmentioning
confidence: 99%