G
Gorka Elordi
Researcher at University of the Basque Country
Publications - 36
Citations - 2760
Gorka Elordi is an academic researcher from University of the Basque Country. The author has contributed to research in topics: Pyrolysis & High-density polyethylene. The author has an hindex of 22, co-authored 35 publications receiving 2167 citations.
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Journal ArticleDOI
Catalytic Pyrolysis of High Density Polyethylene on a HZSM-5 Zeolite Catalyst in a Conical Spouted Bed Reactor
TL;DR: In this paper, the degradation rate of the plastic is slightly faster at 500 °C than at 450 °C and much faster than thermal pyrolysis in both cases using HZSM-5 zeolite as a catalyst.
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Lessening coke formation and boosting gasoline yield by incorporating scrap tire pyrolysis oil in the cracking conditions of an FCC unit
Elena Rodríguez,Sepideh Izaddoust,José Valecillos,Javier Bilbao,José M. Arandes,Pedro Castaño,Pedro Castaño,Eva Epelde,Gorka Elordi +8 more
TL;DR: In this article, the effect of adding scrap tire pyrolysis oil (STPO) as feed or co-feed in the cracking of vacuum gasoil (VGO) using a commercial equilibrated catalyst was studied.
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Characterization of the Liquid Obtained in Tyre Pyrolysis in a Conical Spouted Bed Reactor
TL;DR: In this article, pyrolysis of used tyres has been carried out in a conical spouted bed reactor at 500 ◦C and the liquid product has been characterized taking into account composition, heat value and simulated distillation.
A conical spouted bed reactor for the valorisation of waste tires
TL;DR: In this paper, the effect of pyrolysis temperature on product distribution and properties has been studied in the temperature range from 425 to 600 oC. This variable has proven to have an important effect on product distributions.
Journal ArticleDOI
Imaging the Profiles of Deactivating Species on the Catalyst used for the Cracking of Waste Polyethylene by Combined Microscopies
TL;DR: In this paper, the authors have shown that the external coke grows faster than the internal coke and it is directly responsible for the final collapse of the activity of the catalytic particle.