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Advanced redox flow fuel cell using ferric chloride as main catalyst for complete conversion from carbohydrates to electricity
Liquid catalyzed fuel cell (LCFC) is a kind of redox flow fuel cell directly converting carbohydrates to electricity. To improve its efficiency, ferric chloride (FeCl 3 ) was introduced as main catalyst. As mono catalyst, phosphomolybdic acid (PMo 12 ) was much better than phosphotungstic acid (PW 1...
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Published in: | Scientific reports 2017-07, Vol.7 (1), p.5142-9, Article 5142 |
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Main Authors: | , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | Liquid catalyzed fuel cell (LCFC) is a kind of redox flow fuel cell directly converting carbohydrates to electricity. To improve its efficiency, ferric chloride (FeCl
3
) was introduced as main catalyst. As mono catalyst, phosphomolybdic acid (PMo
12
) was much better than phosphotungstic acid (PW
12
) and FeCl
3
was intermediate between them. Compared with PMo
12
at the optimal dose of 0.30 mol/L, the combination of FeCl
3
(1.00 mol/L) and PW
12
(0.06 mol/L) achieved similar power output from glucose (2.59 mW/cm
2
) or starch (1.57 mW/cm
2
), and even improved the maximum power density by 57% from 0.46 to 0.72 mW/cm
2
when using cellulose as the fuel. Long-term continuous operation of the LCFC indicated that carbohydrates can be hydrolyzed to glucose and then oxidized stepwise to carbon dioxide. At the latter stage, there was a linear relationship between the electron transfer number from glucose to catalyst and the subsequent cell performance. Based on these findings, the contribution of FeCl
3
to LCFC should be derived from the accelerated hydrolysis and oxidation of carbohydrates and the enhanced electron transfer from glucose to anode. The addition of FeCl
3
reduced the usage of polyoxometalates by 80%, and the replacement implied that LCFC can be operated less toxically and more economically. |
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ISSN: | 2045-2322 2045-2322 |
DOI: | 10.1038/s41598-017-05535-2 |