2011
DOI: 10.1016/j.cattod.2011.04.019
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Enhanced hydrogen production by in situ CO2 removal on CaCeZrOx nanocrystals

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Cited by 43 publications
(14 citation statements)
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“…The typical profiles of molar fractions (dry basis) of various species at the outlet of the reactor are given in Supporting Information Figure S4. Three distinct regions, prebreakthrough, breakthrough, and postbreakthrough, are observed as usual . The molar fractions of H 2 , CH 4 , CO, and CO 2 during the prebreakthrough period are measured to be 95.0, 0.6, 2.3, and 2.1%, respectively, which agree well with the corresponding equilibrium molar fractions (by thermodynamic calculation under the same experimental condition), being 94.5, 0.6, 2.4, and 2.5%, respectively.…”
Section: Resultssupporting
confidence: 81%
See 1 more Smart Citation
“…The typical profiles of molar fractions (dry basis) of various species at the outlet of the reactor are given in Supporting Information Figure S4. Three distinct regions, prebreakthrough, breakthrough, and postbreakthrough, are observed as usual . The molar fractions of H 2 , CH 4 , CO, and CO 2 during the prebreakthrough period are measured to be 95.0, 0.6, 2.3, and 2.1%, respectively, which agree well with the corresponding equilibrium molar fractions (by thermodynamic calculation under the same experimental condition), being 94.5, 0.6, 2.4, and 2.5%, respectively.…”
Section: Resultssupporting
confidence: 81%
“…Most investigations on the SESMR process are conducted using individual catalyst and sorbent particles, that is, catalyst and sorbent (two different particles) are physically mixed and then loaded into a reactor . CaO is the most commonly employed sorbent due to its low cost, wide availability, high CO 2 capture capacity, and high carbonation rate .…”
Section: Introductionmentioning
confidence: 99%
“…On the other hand, new synthetic nanomaterials have been developed to improve hydrothermal stability of CO 2 acceptors, such as synthetic mesoporous CaO44 and CaO‐based materials doped with inert but stable oxides (e.g. CeO, ZrO 2 , Al 2 O 3 or TiO 2 ) 45, 46. The synthetic CaO‐based acceptors with large pores, small CaO crystals and surface dopants, such as CaOAl 2 O 3 and CaOCeZrO x mixed oxides, are found to have good kinetics and cyclic stability in ex situ CO 2 capture,46, 47 as well as in situ CO 2 capture during SESR of methane 46, 48…”
Section: Methodsmentioning
confidence: 99%
“…Al 2 O 3 [13][14][15], MgO [16], KMnO 4 [17], CaTiO 3 [18], Ca 12 Al 14 O 33 [19][20][21], Ca 9 Al 6 O 18 [22,23]. Despite good performance in CO 2 sorption, these sorbents are not always applicable to SE-SR due to the presence of steam which would accelerate their deactivation [24]. In [23] the sorbent Ca 9 Al 6 O 18 [22] was tested in SE-SR, obtaining good results in terms of hydrogen purity and sorption capacity.…”
Section: Introductionmentioning
confidence: 92%