A sequential process for hydrogen production based on continuous HDPE fast pyrolysis and in-line steam reforming
A continuous process has been developed consisting in the flash pyrolysis (500 ºC) of high density polyethylene (HDPE) in a conical spouted bed reactor (CSBR) followed by steam reforming in a fluidized bed reactor (Ni commercial catalyst). The effect reforming temperature in the 600-700 ºC range, sp...
| Autores: | , , , , , , |
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| Tipo de recurso: | artículo |
| Fecha de publicación: | 2016 |
| País: | España |
| Institución: | Universidad del País Vasco |
| Repositorio: | Addi. Archivo Digital para la Docencia y la Investigación |
| OAI Identifier: | oai:addi.ehu.eus:10810/65979 |
| Acceso en línea: | http://hdl.handle.net/10810/65979 |
| Access Level: | acceso abierto |
| Palabra clave: | hydrogen pyrolysis reforming plastic waste conical spouted bed Ni catalyst |
| Sumario: | A continuous process has been developed consisting in the flash pyrolysis (500 ºC) of high density polyethylene (HDPE) in a conical spouted bed reactor (CSBR) followed by steam reforming in a fluidized bed reactor (Ni commercial catalyst). The effect reforming temperature in the 600-700 ºC range, space time from 2.8 to 20.8 gcat min gHDPE-1 and steam/plastic ratio between 3 and 5 have on product yields and gas composition has been studied. The continuous pyrolysis-reforming process performs well, with no operational problems and attaining complete HDPE conversion. Under the optimum conditions, i.e., 700 ºC, space time 16.7 gcat min gHDPE-1 and steam/plastic of ratio 5, the H2 yield was 92.5 % of that corresponding to stoichometry, which accounts for a H2 production of 38.1 g per 100g of HDPE in the feed. |
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