Catalytic Properties and Recycling of NiFe<sub>2</sub>O<sub>4</sub> Catalyst for Hydrogen Production by Supercritical Water Gasification of Eucalyptus Wood Chips

Nickel iron oxide (NiFe<sub>2</sub>O<sub>4</sub>) catalyst was prepared by the combustion reaction method and characterized by XRD, N<sub>2</sub> adsorption/desorption, thermogravimetric analysis (TG), and temperature programmed reduction (TPR). The catalyst prese...

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Main Authors: Ane Caroline Pereira Borges, Jude Azubuike Onwudili, Heloysa Andrade, Carine Alves, Andrew Ingram, Silvio Vieira de Melo, Ednildo Torres
Format: Article
Language:English
Published: MDPI AG 2020-09-01
Series:Energies
Subjects:
Online Access:https://www.mdpi.com/1996-1073/13/17/4553
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author Ane Caroline Pereira Borges
Jude Azubuike Onwudili
Heloysa Andrade
Carine Alves
Andrew Ingram
Silvio Vieira de Melo
Ednildo Torres
author_facet Ane Caroline Pereira Borges
Jude Azubuike Onwudili
Heloysa Andrade
Carine Alves
Andrew Ingram
Silvio Vieira de Melo
Ednildo Torres
author_sort Ane Caroline Pereira Borges
collection DOAJ
description Nickel iron oxide (NiFe<sub>2</sub>O<sub>4</sub>) catalyst was prepared by the combustion reaction method and characterized by XRD, N<sub>2</sub> adsorption/desorption, thermogravimetric analysis (TG), and temperature programmed reduction (TPR). The catalyst presented a mixture of oxides, including the NiFe<sub>2</sub>O<sub>4</sub> spinel and specific surface area of 32.4 m<sup>2</sup> g<sup>−1</sup>. The effect of NiFe<sub>2</sub>O<sub>4</sub> catalyst on the supercritical water gasification (SCWG) of eucalyptus wood chips was studied in a batch reactor at 450 and 500 °C without catalyst and with 1.0 g and 2.0 g of catalyst and 2.0 g of biomass for 60 min. In addition, the recyclability of the catalyst under the operating conditions was also tested using recovered and recalcined catalysts over three reaction cycles. The highest amount of H<sub>2</sub> was 25 mol% obtained at 450 °C, using 2 g of NiFe<sub>2</sub>O<sub>4</sub> catalyst. The H<sub>2</sub> mol% was enhanced by 45% when compared to the non-catalytic test, showing the catalytic activity of NiFe<sub>2</sub>O<sub>4</sub> catalyst in the WGS and the steam reforming reactions. After the third reaction cycle, the results of XRD demonstrated formation of coke which caused the deactivation of the NiFe<sub>2</sub>O<sub>4</sub> and consequently, a 13.6% reduction in H<sub>2</sub> mol% and a 5.6% reduction in biomass conversion.
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spelling doaj.art-2bfb1ca02d7a472cbba62fcbba56c27a2023-11-20T12:21:08ZengMDPI AGEnergies1996-10732020-09-011317455310.3390/en13174553Catalytic Properties and Recycling of NiFe<sub>2</sub>O<sub>4</sub> Catalyst for Hydrogen Production by Supercritical Water Gasification of Eucalyptus Wood ChipsAne Caroline Pereira Borges0Jude Azubuike Onwudili1Heloysa Andrade2Carine Alves3Andrew Ingram4Silvio Vieira de Melo5Ednildo Torres6Centro Interdisciplinar em Energia e Ambiente (CIENAM), Campus Universitário Federação/Ondina, Universidade Federal da Bahia (UFBA), Salvador 40170-115, BrazilEnergy and Bioproducts Research Institute, College of Engineering and Physical Sciences, Aston University, Birmingham B4 7ET, UKCentro Interdisciplinar em Energia e Ambiente (CIENAM), Campus Universitário Federação/Ondina, Universidade Federal da Bahia (UFBA), Salvador 40170-115, BrazilCentro Interdisciplinar em Energia e Ambiente (CIENAM), Campus Universitário Federação/Ondina, Universidade Federal da Bahia (UFBA), Salvador 40170-115, BrazilSchool of Chemical Engineering, University of Birmingham, Birmingham B15 2TT, UKCentro Interdisciplinar em Energia e Ambiente (CIENAM), Campus Universitário Federação/Ondina, Universidade Federal da Bahia (UFBA), Salvador 40170-115, BrazilCentro Interdisciplinar em Energia e Ambiente (CIENAM), Campus Universitário Federação/Ondina, Universidade Federal da Bahia (UFBA), Salvador 40170-115, BrazilNickel iron oxide (NiFe<sub>2</sub>O<sub>4</sub>) catalyst was prepared by the combustion reaction method and characterized by XRD, N<sub>2</sub> adsorption/desorption, thermogravimetric analysis (TG), and temperature programmed reduction (TPR). The catalyst presented a mixture of oxides, including the NiFe<sub>2</sub>O<sub>4</sub> spinel and specific surface area of 32.4 m<sup>2</sup> g<sup>−1</sup>. The effect of NiFe<sub>2</sub>O<sub>4</sub> catalyst on the supercritical water gasification (SCWG) of eucalyptus wood chips was studied in a batch reactor at 450 and 500 °C without catalyst and with 1.0 g and 2.0 g of catalyst and 2.0 g of biomass for 60 min. In addition, the recyclability of the catalyst under the operating conditions was also tested using recovered and recalcined catalysts over three reaction cycles. The highest amount of H<sub>2</sub> was 25 mol% obtained at 450 °C, using 2 g of NiFe<sub>2</sub>O<sub>4</sub> catalyst. The H<sub>2</sub> mol% was enhanced by 45% when compared to the non-catalytic test, showing the catalytic activity of NiFe<sub>2</sub>O<sub>4</sub> catalyst in the WGS and the steam reforming reactions. After the third reaction cycle, the results of XRD demonstrated formation of coke which caused the deactivation of the NiFe<sub>2</sub>O<sub>4</sub> and consequently, a 13.6% reduction in H<sub>2</sub> mol% and a 5.6% reduction in biomass conversion.https://www.mdpi.com/1996-1073/13/17/4553catalytic gasificationsupercritical waterhydrogen productionnickel iron oxiderecycling tests
spellingShingle Ane Caroline Pereira Borges
Jude Azubuike Onwudili
Heloysa Andrade
Carine Alves
Andrew Ingram
Silvio Vieira de Melo
Ednildo Torres
Catalytic Properties and Recycling of NiFe<sub>2</sub>O<sub>4</sub> Catalyst for Hydrogen Production by Supercritical Water Gasification of Eucalyptus Wood Chips
Energies
catalytic gasification
supercritical water
hydrogen production
nickel iron oxide
recycling tests
title Catalytic Properties and Recycling of NiFe<sub>2</sub>O<sub>4</sub> Catalyst for Hydrogen Production by Supercritical Water Gasification of Eucalyptus Wood Chips
title_full Catalytic Properties and Recycling of NiFe<sub>2</sub>O<sub>4</sub> Catalyst for Hydrogen Production by Supercritical Water Gasification of Eucalyptus Wood Chips
title_fullStr Catalytic Properties and Recycling of NiFe<sub>2</sub>O<sub>4</sub> Catalyst for Hydrogen Production by Supercritical Water Gasification of Eucalyptus Wood Chips
title_full_unstemmed Catalytic Properties and Recycling of NiFe<sub>2</sub>O<sub>4</sub> Catalyst for Hydrogen Production by Supercritical Water Gasification of Eucalyptus Wood Chips
title_short Catalytic Properties and Recycling of NiFe<sub>2</sub>O<sub>4</sub> Catalyst for Hydrogen Production by Supercritical Water Gasification of Eucalyptus Wood Chips
title_sort catalytic properties and recycling of nife sub 2 sub o sub 4 sub catalyst for hydrogen production by supercritical water gasification of eucalyptus wood chips
topic catalytic gasification
supercritical water
hydrogen production
nickel iron oxide
recycling tests
url https://www.mdpi.com/1996-1073/13/17/4553
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