2019
DOI: 10.1016/j.biortech.2019.121647
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Co-pyrolysis of sugarcane bagasse and polystyrene with ex-situ catalytic bed of metal oxides/HZSM-5 with focus on liquid yield

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Cited by 59 publications
(13 citation statements)
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“…More specifically, the positive effects attached to CaO were not only responsible for promoting the dehydration and dehydrogenation reactions of acids and phenols, but also for the production of a more environmentally friendly gas because of the in-situ CO 2 -capture effect associated with CaO carbonation. Although the results of catalytic co-pyrolysis are very encouraging, most of the work in this field has been carried out in micro and lab-scale reactors [31][32][33][34][35][36][37], and the demonstration of this process on a larger scale is still limited [38]. Therefore, the study of this upgrading strategy to a larger scale (Technology Readiness Levels, TRL ≥ (5)) seems necessary as a first step towards the implementation of the catalytic co-pyrolysis processes of lignocellulosic biomass with waste plastics in future bio-refineries.…”
Section: Of 17mentioning
confidence: 99%
“…More specifically, the positive effects attached to CaO were not only responsible for promoting the dehydration and dehydrogenation reactions of acids and phenols, but also for the production of a more environmentally friendly gas because of the in-situ CO 2 -capture effect associated with CaO carbonation. Although the results of catalytic co-pyrolysis are very encouraging, most of the work in this field has been carried out in micro and lab-scale reactors [31][32][33][34][35][36][37], and the demonstration of this process on a larger scale is still limited [38]. Therefore, the study of this upgrading strategy to a larger scale (Technology Readiness Levels, TRL ≥ (5)) seems necessary as a first step towards the implementation of the catalytic co-pyrolysis processes of lignocellulosic biomass with waste plastics in future bio-refineries.…”
Section: Of 17mentioning
confidence: 99%
“…Therefore, the results reported here suggest that the Ga-ZSM-5 is less effective in promoting aromatisation reactions for the polystyrene pyrolysis vapours compared to the other metal-catalysts investigated during copyrolysis. For example, Iftikhar et al [25] suggested that the formation of compounds from the decomposition of biomass was suppressed by polystyrene decomposition intermediates during the co-pyrolysis of biomass (sugarcane bagasse) and polystyrene with metal-ZSM-5 catalysis.…”
Section: Oil Composition From the Co-pyrolysis-catalysis Of Biomass:polystyrenementioning
confidence: 99%
“…Although improvements in the product oil have been reported for copyrolysis of biomass with plastics, the quality is not sufficient for direct use as a fuel and therefore addition of a catalyst, mainly zeolites, has been investigated [22,23]. In particular, there has also been research into the co-pyrolysis of biomass and polystyrene coupled with zeolite catalysis [24][25][26][27][28]. For example, Kumar and Srinivas [27] used a fixed bed slow co-pyrolysis-catalytic reactor for the production of liquid fuels from biomass and polystyrene using spent FCC zeolite catalyst.…”
Section: Introductionmentioning
confidence: 99%
“…Temperature, heating rate and catalyst are key factors in a pyrolysis process [25,26] which when properly manipulated can give the desired high yield and quality of bio-oil which include high pH, low water and ash contents as well as high heating value [27,28]. While the yield of bio-oil is highly linked to temperature influence [29,30] and heating rate [31], bio-oil quality is greatly influenced by catalysts like CaO which is known to increase the oil pH [32] as well as decrease its moisture content [33][34][35][36][37]. In the study of how variables affect a process, the interacting effect is very important.…”
Section: Introductionmentioning
confidence: 99%