2013
DOI: 10.1016/j.apcatb.2012.09.002
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Study on the effect of metal types in (Me)-Al-MCM-41 on the mesoporous structure and catalytic behavior during the vapor-catalyzed co-pyrolysis of pubescens and LDPE

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Cited by 58 publications
(24 citation statements)
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“…In contrast, the influence of high BET surface area of these catalysts on the cracking reactions appeared to be less significant in the pyrolysis of PE/PP mixture. The prominent role of catalyst's acidity observed in our studies is somewhat consistent with the findings reported by Liu et al [27]. Through studying the catalytic performance of different types of MCM-41 in co-pyrolysis of PE and pubescens, they concluded that the catalysts' acidity, rather than the surface area, plays a more significant role in the cracking of primary pyrolytic intermediates.…”
Section: Pyrolysis Yieldssupporting
confidence: 81%
See 1 more Smart Citation
“…In contrast, the influence of high BET surface area of these catalysts on the cracking reactions appeared to be less significant in the pyrolysis of PE/PP mixture. The prominent role of catalyst's acidity observed in our studies is somewhat consistent with the findings reported by Liu et al [27]. Through studying the catalytic performance of different types of MCM-41 in co-pyrolysis of PE and pubescens, they concluded that the catalysts' acidity, rather than the surface area, plays a more significant role in the cracking of primary pyrolytic intermediates.…”
Section: Pyrolysis Yieldssupporting
confidence: 81%
“…The results are in agreement with the observations reported by Aguado et al [26], which showed that the incorporation of aluminum into a siliceous material could perturb the hexagonal ordering of the pores to some extent, giving rise to a wormhole-like structure with a slightly irregular pore arrangement. However, such distorted pore architecture did not appear to have a significant detrimental effect on the catalytic behavior of the mesoporous catalysts, as evidenced by the pyrolysis studies conducted by Liu et al [27].…”
Section: Characterization Of Catalystsmentioning
confidence: 83%
“…[11][12][13] Co-gasification with biomass has also been reported to assist the feeding of gasification of plastics into the gasifier. [14][15][16] In addition, plastics pyrolysis has also been used to produce carbon nanotubes (CNTs), a high-value product having extraordinary physical and chemical properties, by either mixing plastics with catalyst in a single reactor, 17,18 or passing the pyrolysis products of plastics into a second stage catalyst reactor.…”
Section: Introductionmentioning
confidence: 99%
“…Czernik and French [20] investigated the gasification of polypropylene using C11-NK (commercial nickel catalyst), recovering 80% hydrogen of the theoretical potential of polypropylene. Liu et al [13] and Ruoppolo et al [21] carried out the cogasification of biomass/plastic mixtures using Ni loaded -Al 2 O 3 and, Ni and Pd loaded Al-MCM-41(mesoporous aluminosilicates), respectively, which also promoted hydrogen production.…”
Section: Introductionmentioning
confidence: 99%
“…However, the yield of hydrogen from biomass is typically low, therefore, addition of plastics which have a high hydrogen content into the biomass feedstock would enhance the amount of hydrogen in the gaseous product stream. Co-pyrolysis for hydrogen production was reported with various biomass-plastic combinations, such as wood-polypropylene [11], pine cone-polypropylene, pine cone-polyethylene, and pine cone-polystyrene [12], and pubescens-low density polyethylene [13]. These investigations were carried out using various reactors such as a fixed-bed reactor, fluidized-bed reactor, spouted-bed reactor, screw kiln reactor, and molten carbonate reactor, however, which are often combined with catalysts in order to improve the hydrogen production.…”
Section: Introductionmentioning
confidence: 99%