1988
DOI: 10.1016/0144-4565(88)90016-9
|View full text |Cite
|
Sign up to set email alerts
|

Furfural decarbonylation catalyzed by charcoal supported palladium: Part I — Kinetics

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

0
12
0

Year Published

2002
2002
2024
2024

Publication Types

Select...
8

Relationship

0
8

Authors

Journals

citations
Cited by 28 publications
(12 citation statements)
references
References 7 publications
0
12
0
Order By: Relevance
“…Conducting the reaction in the liquid phase results in less intense deactivation processes and in a more viable process. 381,[384][385][386] Furan has a low boiling point (304 K), and therefore, furan is continuously distilled at the reaction temperature. A Pd/C catalyst promoted by K 2 CO 3 was identified as the best catalyst.…”
Section: Liquid-phase Decarbonylationmentioning
confidence: 99%
“…Conducting the reaction in the liquid phase results in less intense deactivation processes and in a more viable process. 381,[384][385][386] Furan has a low boiling point (304 K), and therefore, furan is continuously distilled at the reaction temperature. A Pd/C catalyst promoted by K 2 CO 3 was identified as the best catalyst.…”
Section: Liquid-phase Decarbonylationmentioning
confidence: 99%
“…Gaset et al [61][62][63][64] performed the decarbonylation reaction at a milder temperature (160 8C) in the liquid phase in the absence of H 2 using Al 2 O 3 -and C-supported Pd catalysts and K 2 CO 3 as the cocatalyst. The reaction was not affected by traces of water, but was hindered by traces of acids, which were formed, for example, by autooxidation of furfural during storage.…”
Section: Decarbonylationmentioning
confidence: 99%
“…As early as 2012, Huber and Cheng synthesized toluene and benzene by co-adding ethylene or propylene with FF at 450-600 °C and in situ decarbonylation of FF in the presence of ZSM-5, but obtained the corresponding unsatisfactory results. 103 In contrast, reductive decarbonylation was carried out in the gas phase 102 or liquid phase 104,105 at 250-300 °C or lower temperature conditions. The decarbonylation in the gas phase proceeded with a supported precious metal catalyst in the presence of H 2 , which demonstrated the advantages of high yield and a relatively simple catalyst cycle and regeneration.…”
Section: Indirect Da Reaction Strategy Of Ff and Hmfmentioning
confidence: 99%