2010
DOI: 10.1016/j.fuproc.2010.05.017
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Catalytic degradation of waste high-density polyethylene into fuel products using BaCO3 as a catalyst

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Cited by 75 publications
(34 citation statements)
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“…The liquid products are distributed in C 5 -C 20 range, that is, basically in the gasoline and diesel ranges. The effect of nonacidic catalysts for the pyrolysis of plastics was studied by Jan et al [6]. On comparison with MgCO 3 when used as a catalyst under 450 ∘ C, it could be observed that the % oil yield (33.60%) is higher with MgCO 3 as compared to the % oil yield (29.60%) obtained with BaCO 3 catalyst.…”
Section: Effect Of Catalystmentioning
confidence: 99%
“…The liquid products are distributed in C 5 -C 20 range, that is, basically in the gasoline and diesel ranges. The effect of nonacidic catalysts for the pyrolysis of plastics was studied by Jan et al [6]. On comparison with MgCO 3 when used as a catalyst under 450 ∘ C, it could be observed that the % oil yield (33.60%) is higher with MgCO 3 as compared to the % oil yield (29.60%) obtained with BaCO 3 catalyst.…”
Section: Effect Of Catalystmentioning
confidence: 99%
“…The medium pore SAPOs are attractive for catalytic applications due to the presence of specific acid sites in its structure which can convert the polymer into useful hydrocarbons (Elordi et al, 2009, Singhal et al, 2010. The use of BaCO 3 as a catalyst for the thermal and catalytic degradation of waste HDPE was also reported (Rasul Jan et al, 2010).…”
Section: Catalytic Degradationmentioning
confidence: 99%
“…The gases and oils were collected using different bladder and vessels separately, and this pyrolysis reactor was used to degrade the high‐density polyethylene (HDPE) using BaCO 3 and CaCO 3 as catalysts that gave low wax formation and hydrocarbons with minimized boiling point. It indicates that continuous cracking taking place in a long‐chain hydrocarbon generated from thermal degradations and the catalyzed oil fractions properties resembled with standard petroleum products such as gasoline, kerosene, and diesel with temperatures of 100, 150, and 250 °C, respectively . The catalytic fluidized process was carried out with waste consumer plastic bottles form hospitals in a temperature range of 330 to 450 °C with various catalysts, and the zeolite‐based fluid catalytic cracking (FCC)‐R1 catalyst at 390 °C gave more gasoline fractions (54.8 wt.% of C 4 –C 9 and 24.3 wt.% of C 1 –C 4 ) with reasonable conversion efficiency.…”
Section: Introductionmentioning
confidence: 99%
“…Schematic diagram for thermal degradation setup (reprinted with permission from Rasul et al . . Copyright Elsevier, 2010).…”
Section: Introductionmentioning
confidence: 99%