2011
DOI: 10.1016/j.ijhydene.2011.02.008
|View full text |Cite
|
Sign up to set email alerts
|

Iron and nickel doped alkaline-earth catalysts for biomass gasification with simultaneous tar reformation and CO2 capture

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1
1

Citation Types

0
52
0
1

Year Published

2013
2013
2020
2020

Publication Types

Select...
8
2

Relationship

0
10

Authors

Journals

citations
Cited by 116 publications
(53 citation statements)
references
References 39 publications
0
52
0
1
Order By: Relevance
“…Domínguez et al [41] studied the pyrolysis of sewage sludge and reported that a high concentration of metals, especially for iron, would favor reactions between the metals and organic compounds, promoting tar cracking to generate more gaseous products. An enhanced hydrogen production was observed with the presence of Iron/Nickel-loaded catalysts [42] or nickel-coated distributor of the gasifier [43]. Therefore, it suggests that the Fig.…”
Section: Gas Compositionmentioning
confidence: 90%
“…Domínguez et al [41] studied the pyrolysis of sewage sludge and reported that a high concentration of metals, especially for iron, would favor reactions between the metals and organic compounds, promoting tar cracking to generate more gaseous products. An enhanced hydrogen production was observed with the presence of Iron/Nickel-loaded catalysts [42] or nickel-coated distributor of the gasifier [43]. Therefore, it suggests that the Fig.…”
Section: Gas Compositionmentioning
confidence: 90%
“…It is reported that Ni and Fe can greatly catalyze the gasification process. Di Felice et al [40] synthesized Fe and Ni doped alkaline-earth catalysts for biomass gasification. It was concluded that an enhanced hydrogen production was favored with the presence of Fe and Ni.…”
Section: Gasification Characteristicsmentioning
confidence: 99%
“…Elemental analyses were carried out on the used catalysts in order to quantify these carbon deposits. The amount of coke deposited on the catalysts during two hours of reaction, expressed as mg C/ g catalyst g organics reacted [37], has been calculated and statistically compared. This comparison shows that the carbon content deposited on the catalyst was higher for the two aqueous fractions obtained from the bio-oils whose pyrolysis took place in the fluidised bed (15528 and 1488 mg C/g catalyst g organics reacted for the pine and the poplar, respectively) than for those whose pyrolysis was carried out in the spouted bed reactor (9612 and 955 mg C/g catalyst g organics reacted for the pine and the poplar, respectively).…”
Section: Coke Deposition On the Catalystmentioning
confidence: 99%