Energy generation by air gasification of two industrial plastic wastes in a pilot scale fluidized bed reactor
Two plastic wastes obtained as co-products from an industrial process were fed in a pilot-scale bubbling fluidized bed gasifier, having an internal diameter of 0.38 m and a maximum thermal output of about 400 kW. The experimental runs were carried out by reaching a condition of thermal and chemical steady state under values of equivalence ratio ranging from 0.2 to 0.3. Olivine, a neo-silicate of Fe and Mg, already tested as a good catalyst for tar removal during gasification of polyolefin plastic wastes, was used as bed material. The results provide the complete composition of the syngas, including the tar, particulate and acid/basic gas contents as well as the chemical and physical characterization of the bed material and entrained fines. The gasification process appears technically feasible, yielding a producer gas of valuable quality for energy applications in an appropriate plant configuration. On the other hand, under the experimental conditions tested, olivine particles show a strongly reduced catalytic activity in all the runs. The differences in the gasification behaviour of the two industrial plastics are explained on the basis of the structure and composition of the wastes, taking also into account the results of a combined material and substance flow analysis.
Year of publication: |
2014
|
---|---|
Authors: | Arena, Umberto ; Di Gregorio, Fabrizio |
Published in: |
Energy. - Elsevier, ISSN 0360-5442. - Vol. 68.2014, C, p. 735-743
|
Publisher: |
Elsevier |
Subject: | Gasification | Mixed-plastic waste | Fluidized bed | Waste-to-energy | Co-gasification |
Saved in:
Online Resource
Saved in favorites
Similar items by subject
-
Eco-innovations in waste management : a review of high point cases
Manasi, S., (2020)
-
Di Gregorio, F., (2012)
-
Pilot study on jetting pre-oxidation fluidized bed gasification adapting to caking coal
Zhang, Juwei, (2013)
- More ...