Conversion of low density polyethylene into fuel through co-processing with vacuum gas oil in a fluid catalytic cracking riser reactor
Empreu sempre aquest identificador per citar o enllaçar aquest ítem
http://hdl.handle.net/10045/40344
Títol: | Conversion of low density polyethylene into fuel through co-processing with vacuum gas oil in a fluid catalytic cracking riser reactor |
---|---|
Autors: | Odjo, Andrew O. | García, Angela N. | Marcilla, Antonio |
Grups d'investigació o GITE: | Procesado y Pirólisis de Polímeros |
Centre, Departament o Servei: | Universidad de Alicante. Departamento de Ingeniería Química | Universidad de Alicante. Instituto Universitario de Ingeniería de los Procesos Químicos |
Paraules clau: | Vacuum gas oil | Polyethylene | Fluid catalytic cracking | Riser reactor | FCC catalyst |
Àrees de coneixement: | Ingeniería Química |
Data de publicació: | de setembre-2013 |
Editor: | Elsevier |
Citació bibliogràfica: | Fuel Processing Technology. 2013, 113: 130-140. doi:10.1016/j.fuproc.2013.03.008 |
Resum: | In this work, mixtures of vacuum gas oil and low density polyethylene, a major component of common industrial and consumer household plastics, were pyrolytically co-processed in a fluid catalytic cracking (FCC) riser reactor as a viable alternative for the energy and petrochemical revalorisation of plastic wastes into valuable petrochemical feedstocks and fuel within an existing industrial technology. Using equilibrium FCC catalyst, the oil–polymer blends were catalytically cracked at different processing conditions of temperatures between 773 K and 973 K and catalyst feed ratios of 5:1, 7:1 and 10:1. The influence of each of these processing parameters on the cracking gas and liquid yield patterns were studied and presented. Further analysed and presented are the different compositional distributions of the obtained liquids and gaseous products. The analysis of the results obtained revealed that with very little modifications to existing process superstructure, yields and compositional distributions of products from the fluid catalytic cracking of the oil–polymer blend in many cases were very similar to those of the processed oil feedstock, bringing to manifest the viability of the feedstock co-processing without significant detriments to FCC product yields and quality. |
Patrocinadors: | The authors gratefully acknowledge the financial support from the Spanish Generalitat Valenciana (GVEMP06/021 and PROMETEO/2012/015), the Ministry of Science and Technology (project CTQ2004-02187) and the Ministry of Economy and Competitivity (project MAT2011-24991). |
URI: | http://hdl.handle.net/10045/40344 |
ISSN: | 0378-3820 (Print) | 1873-7188 (Online) |
DOI: | 10.1016/j.fuproc.2013.03.008 |
Idioma: | eng |
Tipus: | info:eu-repo/semantics/article |
Revisió científica: | si |
Versió de l'editor: | http://dx.doi.org/10.1016/j.fuproc.2013.03.008 |
Apareix a la col·lecció: | INV - GTP3 - Artículos de Investigación sobre Pirólisis Catalítica de Polímeros |
Arxius per aquest ítem:
Arxiu | Descripció | Tamany | Format | |
---|---|---|---|---|
2013_Odjo_etal_FPT_final.pdf | Versión final (acceso restringido) | 4 MB | Adobe PDF | Obrir Sol·licitar una còpia |
Tots els documents dipositats a RUA estan protegits per drets d'autors. Alguns drets reservats.