2010
DOI: 10.1016/j.wasman.2009.10.001
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Valorisation of waste tyre by pyrolysis in a moving bed reactor

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Cited by 143 publications
(65 citation statements)
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“…In a further stage, the effects of various parameters were examined for their effect on product yield including temperature, solid residence time and inner gas flow rate in a screw kiln reactor [105]. They observed maximum oil yield of 48.4 wt % at 600 • C with a throughput of 8 kg·h −1 .…”
Section: Moving-bed Reactor Pyrolysismentioning
confidence: 99%
“…In a further stage, the effects of various parameters were examined for their effect on product yield including temperature, solid residence time and inner gas flow rate in a screw kiln reactor [105]. They observed maximum oil yield of 48.4 wt % at 600 • C with a throughput of 8 kg·h −1 .…”
Section: Moving-bed Reactor Pyrolysismentioning
confidence: 99%
“…A static bed reactor, autoclave, or rotary kiln doesn't need any particular load size, just small enough to be filled during the experiments. In the fluidized bed reactor usually a size of 1-2 mm (Kaminsky & Mennerich, 2001), 2 mm or no more than 5 mm (Aylón et al, 2010) is required. The limitations displayed above are held back controlling the other experiment's variables: pyrolysis running time, apparatus set-up and material flux.…”
Section: Microwave or Non-microwave Heating In Pyrolysis Processes: Tmentioning
confidence: 99%
“…Algeria alone generates approximately 25918.50 tons/year of used tires [1]. Numerous technical solutions and integrated management system related to end of life tyres are proposed [2][3][4][5][6].…”
Section: Introductionmentioning
confidence: 99%