2016
DOI: 10.1016/j.ijhydene.2016.05.232
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The impact of physicochemical properties of coal on direct carbon solid oxide fuel cells

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Cited by 16 publications
(10 citation statements)
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“…It seems that Al 2 O 3 and SiO 2 , together with CaO, K 2 O and Fe 2 O 3 , could form deposits on the catalyst surface and obstruct the pores [112] . Generally, a negative effect of high ash contents in the biomass on the DCFC performance and durability was observed [117–121] . Indeed, a high content of ash hinder the contact between the carbon particles and the anode, leading to the blockage of anode active sites.…”
Section: Direct Biomass (Lignocellulose Cellulose and Lignin) Fuel mentioning
confidence: 99%
“…It seems that Al 2 O 3 and SiO 2 , together with CaO, K 2 O and Fe 2 O 3 , could form deposits on the catalyst surface and obstruct the pores [112] . Generally, a negative effect of high ash contents in the biomass on the DCFC performance and durability was observed [117–121] . Indeed, a high content of ash hinder the contact between the carbon particles and the anode, leading to the blockage of anode active sites.…”
Section: Direct Biomass (Lignocellulose Cellulose and Lignin) Fuel mentioning
confidence: 99%
“…33,34 The r 2 can be controlled by tuning the current densities; however, the r 1 normally decreases due to carbon consumption and other reasons. [33][34][35][36][37][38][39][40][41][42][43][44] The reverse Boudouard reaction is an endothermic reaction with the free energy change expressed as ΔG (kJ mol −1 ) = 170 − 0.1745T, where T is temperature in°K . The CO formation is strongly favored at temperatures above 974.2 K. 6 From the viewpoints of thermodynamics and kinetics, elevated temperatures are the key factor that determines the rate of Boudouard reaction to reach equilibrium and the partial press of CO in the system.…”
Section: Introductionmentioning
confidence: 99%
“…The diffusion rates of CO and CO 2 , ie, r d 1 and r d 2 , respectively, have been proved to be much faster than the rates of R1 and R2; hence, the diffusion processes have almost no impeding effect on the cell performance . The r 2 can be controlled by tuning the current densities; however, the r 1 normally decreases due to carbon consumption and other reasons …”
Section: Introductionmentioning
confidence: 99%
“…Recently, the feasibility of coal as fuel for DC‐SOFCs has attracted more and more attentions . The peak power density (PPD) of 89 mW cm −2 at 800°C was observed for the char of brown coal in DC‐SOFCs .…”
Section: Introductionmentioning
confidence: 99%
“…22 Recently, the feasibility of coal as fuel for DC-SOFCs has attracted more and more attentions. [23][24][25][26][27][28][29][30] The peak power density (PPD) of 89 mW cm −2 at 800°C was observed for the char of brown coal in DC-SOFCs. 24 An electrolyte supported SOFC using the lignite and lignite char as fuel reached the respective PPDs of 93 and 143 mW cm −2 both operating at 850°C.…”
Section: Introductionmentioning
confidence: 99%