Title
|
|
|
|
Chemical looping syngas from and over manganese oxide minerals
|
|
Author
|
|
|
|
|
|
Abstract
|
|
|
|
Rather than sequestering carbon dioxide from the exhaust of chemical looping combustion reactors, together with the water, it could be usedas a source of syngas. For the first time, we split water to hydrogen and carbon dioxide to carbon monoxide with a manganese ore. SpecificCO production is 10–100 times higher than Sr, Ce, and Fe doped perovskites and Y0.5Sr0.5MnO3perovskites. At a contact time of 0.01 sand at temperatures ranging from 810–960◦C the maximum specific CO production was 5.5 mol·kg−1. A combined kinetic-axial dispersionhydrodynamic model accounts for 97 % of the variance in the data assuming the reaction rate is first-order in CO2and surface reduced sites andin equilibrium with the reverse reaction—a first-order reaction in CO with surface oxidized sites. A second reaction accounts for the diffusion ofsurface oxygen to the bulk lattice. Hydrogen productivity peaked at 4.8 mol·kg−1at 947◦C, which is twice as high as reported in previous studieson CoFe2O4and Al2O3in the hercynite cycle. |
|
|
Language
|
|
|
|
English
|
|
Source (journal)
|
|
|
|
The Canadian journal of chemical engineering. - Ottawa, Ont., 1957, currens
|
|
Publication
|
|
|
|
Ottawa, Ont.
:
2016
|
|
ISSN
|
|
|
|
0008-4034
[print]
1939-019X
[online]
|
|
DOI
|
|
|
|
10.1002/CJCE.22432
|
|
Volume/pages
|
|
|
|
94
:4
(2016)
, p. 703-712
|
|
ISI
|
|
|
|
000372556700013
|
|
Full text (Publisher's DOI)
|
|
|
|
|
|
Full text (publisher's version - intranet only)
|
|
|
|
|
|