2011
DOI: 10.1016/j.cattod.2011.04.052
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Catalytic tar removal from bio syngas—Catalyst development and kinetic studies

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Cited by 34 publications
(19 citation statements)
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“…However, in methane oxidation over Y 2 O 3 -ZrO 2 the formation of CO and H 2 increased with increasing temperature (from 500 °C to 1100 °C) [25], while in toluene oxidation (present work) their formation first increased and then started to decrease with increasing temperature (from 200 °C to 600 °C). Another interesting similarity in product formation shapes was reported by Schmidt et al [26] in temperature-programmed oxidation of naphthalene (as a tar model compound) over a Mo/V/W catalyst, the product formation curve shapes obtained for CO 2 and H 2 O were similar to those over ZrO 2 (present work). Also the consumption curves of naphthalene and oxygen over the Mo/V/W catalyst showed a remarkable similarity to the consumption curves of toluene and oxygen over ZrO 2 -based catalysts.…”
Section: Discussionsupporting
confidence: 84%
See 1 more Smart Citation
“…However, in methane oxidation over Y 2 O 3 -ZrO 2 the formation of CO and H 2 increased with increasing temperature (from 500 °C to 1100 °C) [25], while in toluene oxidation (present work) their formation first increased and then started to decrease with increasing temperature (from 200 °C to 600 °C). Another interesting similarity in product formation shapes was reported by Schmidt et al [26] in temperature-programmed oxidation of naphthalene (as a tar model compound) over a Mo/V/W catalyst, the product formation curve shapes obtained for CO 2 and H 2 O were similar to those over ZrO 2 (present work). Also the consumption curves of naphthalene and oxygen over the Mo/V/W catalyst showed a remarkable similarity to the consumption curves of toluene and oxygen over ZrO 2 -based catalysts.…”
Section: Discussionsupporting
confidence: 84%
“…Also the consumption curves of naphthalene and oxygen over the Mo/V/W catalyst showed a remarkable similarity to the consumption curves of toluene and oxygen over ZrO 2 -based catalysts. In addition, Schmidt et al [26] reported that in the presence of hydrogen and carbon monoxide naphthalene was fully converted at 500 °C with negligible conversions of CO and H 2 , yet the possible formation of these two was not reported.…”
Section: Discussionmentioning
confidence: 95%
“…Precious metals are also active for the tar reforming reaction. On a series of precious metal supported CeO 2 -SiO 2 catalysts, Tomishige et al reported that the activity decreased in a sequence of Rh > Pt > Pd (≈Ni) > Ru [21]. However, precious metal catalysts are expensive, making them less practical for tar reforming applications.…”
mentioning
confidence: 99%
“…Between wet and hot gas cleaning, the latter should be preferred since it really destroys the tars instead of transferring them to a liquid phase, which would need further and expensive treatment [29]. Also, for energy efficiency reasons of the whole process, the hot gas cleaning is a promising method [30] and several authors have recently studied this sort of method with successful results [30][31][32][33].…”
Section: Tarmentioning
confidence: 99%