Abstract

A benign route for hydrogen (H2) production is environmentally desirable. To achieve this, H2 synthesis from polymeric waste was investigated. A new route was sought to maximize H2 production with the least formation of coke during catalytic pyrolysis of fishing net waste (FNW) by using CO2 (as reaction media) and a Ni/SiO2 (as catalyst). The thermolytic characteristics of FNW were also evaluated under the CO2 condition (and N2 as reference environment) both with and without catalysts to assess the full scope of variabilities involved in catalytic pyrolysis of FNW. The use of Ni/SiO2 catalyst in each of the N2 and CO2 conditions improved the reaction kinetics in terms of syngas formation with significant production of H2 (1,543 and 770 mmol g−1cat h−1) and CO (11 and 1157 mmol g−1cat h−1), respectively. However, H2 production rate dropped when the catalyst was deactivated due to (hydro)carbon deposition onto the catalyst surface under N2 environment. Under CO2 environment, CO2 served as an oxidant during FNW thermolysis with additional CO formation and prolonged lifetime of catalyst (via suppressed deactivation). H2 production mediated by CO2 increased to ≥1,093 mmol g−1cat h−1 during five repeated cycles of FNW pyrolysis, coupling with water–gas shift reaction (WGS: CO+H2O⇌H2+CO2). This new approach to H2 production is demonstrated as a practical measure for producing H2 while extending catalyst life.

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