2018
DOI: 10.1007/s40090-018-0147-2
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Thermo-catalytic degradation of different plastics to drop in liquid fuel using calcium bentonite catalyst

Abstract: Thermal and catalytic pyrolysis of individual plastics such as polypropylene (PP), low-density polyethylene (LDPE), highdensity polyethylene (HDPE), and mixture of all three plastics (PP + LDPE + HDPE) were carried out in the presence of calcium bentonite as catalyst in a batch reactor to obtain suitable liquid fuel. The dependencies of process temperature, effect of catalyst, feed composition on yield of the fuel fraction were determined. The major product of both thermal and catalytic pyrolysis was condensab… Show more

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Cited by 51 publications
(34 citation statements)
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“…The pyrolysis of HDPE, LDPE, PP and mixed plastics yielded three different products: condensed oil and/or wax, non-condensable gas, and residue. The distribution of these fractions is different at different temperatures from 400 to 550 °C [21]. The condensable oil/ wax and the non-condensable gas/volatiles fractions constituted major products as compared to the solid residue fractions.…”
Section: Effect Of Temperaturementioning
confidence: 96%
“…The pyrolysis of HDPE, LDPE, PP and mixed plastics yielded three different products: condensed oil and/or wax, non-condensable gas, and residue. The distribution of these fractions is different at different temperatures from 400 to 550 °C [21]. The condensable oil/ wax and the non-condensable gas/volatiles fractions constituted major products as compared to the solid residue fractions.…”
Section: Effect Of Temperaturementioning
confidence: 96%
“…[131] Clays have macroporous structures with milder acidity all of which facilitates moderate polymer cracking to produce heavier products. [131,132,221,222] The large porous nature of clays inhibits increased contact of the polymer with active sites, thus allowing for larger products to desorb prior to further reaction and resulting in the production of liquid fuels similar to that of diesel. [131,221,222] However, due to the large pore diameter, coke precursors fail to form and as a result, such catalysts are more deactivation resistant.…”
Section: Claysmentioning
confidence: 99%
“…When HDPE has been used as biomass, the reaction time without catalyst has been 83 minutes, while the reaction time has been reduced to 64 minutes with 33.3% (1:3) catalyst. The specific gravity of the pyrolysis oil measured 0.853 g/cm 3 when using %5 (1:20) catalyst in the pyrolysis process while it measured 0.789 g/cm 3 when using %5 (1:20) catalyst [47]. By using different catalysts and determining the optimum catalyst/biomass ratio, more chemically homogeneous and different ratios of pyrolysis products can be obtained.…”
Section: Catalyst Effectmentioning
confidence: 99%