2018
DOI: 10.1016/j.apcata.2018.07.027
|View full text |Cite
|
Sign up to set email alerts
|

Dry reforming of glycerol over Rh-based ceria and zirconia catalysts: New insights on catalyst activity and stability

Abstract: Effects of reaction temperature and feed composition on reactant conversion, product distribution and catalytic stability were investigated on syngas production by reforming of glycerol, a renewable waste, with CO 2 on Rh/ ZrO 2 and Rh/CeO 2 catalysts. For the first time in the literature, fresh and spent catalysts were characterized by in-situ FTIR, Raman spectroscopy, transmission electron microscopy and energy dispersive X-ray analysis techniques in order to unravel novel insights regarding the molecular-le… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

5
37
0

Year Published

2019
2019
2022
2022

Publication Types

Select...
7
1

Relationship

0
8

Authors

Journals

citations
Cited by 49 publications
(42 citation statements)
references
References 76 publications
(116 reference statements)
5
37
0
Order By: Relevance
“…Methane dry reforming is a thermo-catalytic process used for producing synthetic gas (syngas), a mixture of hydrogen (H 2 ) and carbon monoxide (CO), by utilizing methane (CH 4 ) and carbon dioxide (CO 2 ) as feedstocks [1]. Although there are several processes such as steam methane reforming [2], coal gasification [3], glycerol reforming [4], and partial oxidation reforming [5] that can be employed for syngas production, none of these processes have the advantages of mitigating greenhouse gas emission through the consumption of CH 4 and CO 2 [6]. Besides being a potential technical route for greenhouse gas emission reduction, methane dry reforming has the advantage of producing syngas with a H 2 :CO ratio close to unity [7].…”
Section: Introductionmentioning
confidence: 99%
“…Methane dry reforming is a thermo-catalytic process used for producing synthetic gas (syngas), a mixture of hydrogen (H 2 ) and carbon monoxide (CO), by utilizing methane (CH 4 ) and carbon dioxide (CO 2 ) as feedstocks [1]. Although there are several processes such as steam methane reforming [2], coal gasification [3], glycerol reforming [4], and partial oxidation reforming [5] that can be employed for syngas production, none of these processes have the advantages of mitigating greenhouse gas emission through the consumption of CH 4 and CO 2 [6]. Besides being a potential technical route for greenhouse gas emission reduction, methane dry reforming has the advantage of producing syngas with a H 2 :CO ratio close to unity [7].…”
Section: Introductionmentioning
confidence: 99%
“…Comparing the other two catalysts, it seems that the Ir/CeAl is slightly more selective to H 2 than the Pd/CeAl (for the Ir/CeAl, the S H2 ranges from ≈37 to 63% and the Y H2 from 0.8 to 4.6, from 400 to 750 • C, respectively). These results may indicate that the methanation reaction (at lower temperatures) and the RWGS reaction (at higher temperatures), both leading to the consumption of hydrogen, are more dominant on the Ir/CeAl and Pd/CeAl catalysts [93]. Moreover, the much improved performance of the Pt/CeAl may be related to: (i) the increased number of Brønsted acid sites (as shown by the TPD experiments), which improved the hydrogenolysis and dehydrogenation-dehydration of condensable intermediates, leading to enhanced H 2 production, and (ii) the smaller metal particle size (electron microscopy analysis), which favours the cleavage of the C-C and C-O bonds in the C 3 H 8 O 3 molecules.…”
Section: Catalytic Activity and Selectivitymentioning
confidence: 95%
“…For dry reforming, different catalysts can be used, highlighting Ni, Rh, Ru, Ir, Pd, or Pt [20,[100][101][102][103][104], with coke accumulation and the sintering of catalyst particles (especially for Rh) as the main disadvantages, as in other cases [20]. In order to avoid coke accumulation, La was added to these catalysts to promote active sites, due to its redox property to remove carbon and its lower acidity compared to other popular catalysts such as Ni [100].…”
Section: Dry Reformingmentioning
confidence: 99%
“…Additionally, the use of supports such as MgO and CaO can increase the carbon resistance within the catalyst, reducing carbon deposition [105]. On the other hand, ZrO 2 and CeO 2 represent promising materials as supports for the dry reforming of glycerol, due to their oxygen transfer properties, helping in the dissociation of CO 2 into CO and O [104].…”
Section: Dry Reformingmentioning
confidence: 99%