Stability and Activity of Rhodium Promoted Nickel-Based Catalysts in Dry Reforming of Methane
The rhodium oxide (Rh<sub>2</sub>O<sub>3</sub>) doping effect on the activity and stability of nickel catalysts supported over yttria-stabilized zirconia was examined in dry reforming of methane (DRM) by using a tubular reactor, operated at 800 °C. The catalysts were characte...
Main Authors: | , , , , , , , , , , , |
---|---|
Format: | Article |
Language: | English |
Published: |
MDPI AG
2023-01-01
|
Series: | Nanomaterials |
Subjects: | |
Online Access: | https://www.mdpi.com/2079-4991/13/3/547 |
_version_ | 1797623643852767232 |
---|---|
author | Jehad Saleh Ahmed Sadeq Al-Fatesh Ahmed Aidid Ibrahim Francesco Frusteri Ahmed Elhag Abasaeed Anis Hamza Fakeeha Fahad Albaqi Khalid Anojaidi Salwa B. Alreshaidan Ibrahim Albinali Abdulrahman A. Al-Rabiah Abdulaziz Bagabas |
author_facet | Jehad Saleh Ahmed Sadeq Al-Fatesh Ahmed Aidid Ibrahim Francesco Frusteri Ahmed Elhag Abasaeed Anis Hamza Fakeeha Fahad Albaqi Khalid Anojaidi Salwa B. Alreshaidan Ibrahim Albinali Abdulrahman A. Al-Rabiah Abdulaziz Bagabas |
author_sort | Jehad Saleh |
collection | DOAJ |
description | The rhodium oxide (Rh<sub>2</sub>O<sub>3</sub>) doping effect on the activity and stability of nickel catalysts supported over yttria-stabilized zirconia was examined in dry reforming of methane (DRM) by using a tubular reactor, operated at 800 °C. The catalysts were characterized by using several techniques including nitrogen physisorption, X-ray diffraction, transmission electron microscopy, H<sub>2</sub>-temperature programmed reduction, CO<sub>2</sub>-temperature programmed Desorption, and temperature gravimetric analysis (TGA). The morphology of Ni-YZr was not affected by the addition of Rh<sub>2</sub>O<sub>3</sub>. However, it facilitated the activation of the catalysts and reduced the catalyst’s surface basicity. The addition of 4.0 wt.% Rh<sub>2</sub>O<sub>3</sub> gave the optimum conversions of CH<sub>4</sub> and CO<sub>2</sub> of ~89% and ~92%, respectively. Furthermore, the incorporation of Rh<sub>2</sub>O<sub>3</sub>, in the range of 0.0–4.0 wt.% loading, enhanced DRM and decreased the impact of reverse water gas shift, as inferred by the thermodynamics analysis. TGA revealed that the addition of Rh<sub>2</sub>O<sub>3</sub> diminished the carbon formation on the spent catalysts, and hence, boosted the stability, owing to the potential of rhodium for carbon oxidation through gasification reactions. The 4.0 wt.% Rh<sub>2</sub>O<sub>3</sub> loading gave a 12.5% weight loss of carbon. The TEM images displayed filamentous carbon, confirming the TGA results. |
first_indexed | 2024-03-11T09:31:49Z |
format | Article |
id | doaj.art-dcc8d18af8ef43b0abd76817be453856 |
institution | Directory Open Access Journal |
issn | 2079-4991 |
language | English |
last_indexed | 2024-03-11T09:31:49Z |
publishDate | 2023-01-01 |
publisher | MDPI AG |
record_format | Article |
series | Nanomaterials |
spelling | doaj.art-dcc8d18af8ef43b0abd76817be4538562023-11-16T17:36:20ZengMDPI AGNanomaterials2079-49912023-01-0113354710.3390/nano13030547Stability and Activity of Rhodium Promoted Nickel-Based Catalysts in Dry Reforming of MethaneJehad Saleh0Ahmed Sadeq Al-Fatesh1Ahmed Aidid Ibrahim2Francesco Frusteri3Ahmed Elhag Abasaeed4Anis Hamza Fakeeha5Fahad Albaqi6Khalid Anojaidi7Salwa B. Alreshaidan8Ibrahim Albinali9Abdulrahman A. Al-Rabiah10Abdulaziz Bagabas11Chemical Engineering Department, College of Engineering, King Saud University, P.O. Box 800, Riyadh 11421, Saudi ArabiaChemical Engineering Department, College of Engineering, King Saud University, P.O. Box 800, Riyadh 11421, Saudi ArabiaChemical Engineering Department, College of Engineering, King Saud University, P.O. Box 800, Riyadh 11421, Saudi ArabiaCNR-ITAE, Istituto di Tecnologie Avanzate per Energia “Nicola Giordano”, Via S. Lucia Sopra Contesse 5, 98126 Messina, ItalyChemical Engineering Department, College of Engineering, King Saud University, P.O. Box 800, Riyadh 11421, Saudi ArabiaChemical Engineering Department, College of Engineering, King Saud University, P.O. Box 800, Riyadh 11421, Saudi ArabiaPresident Office, King Abdulaziz City for Science and Technology (KACST), P.O. Box 6086, Riyadh 11442, Saudi ArabiaPresident Office, King Abdulaziz City for Science and Technology (KACST), P.O. Box 6086, Riyadh 11442, Saudi ArabiaDepartment of Chemistry, Faculty of Science, King Saud University, P.O. Box 800, Riyadh 11451, Saudi ArabiaPresident Office, King Abdulaziz City for Science and Technology (KACST), P.O. Box 6086, Riyadh 11442, Saudi ArabiaChemical Engineering Department, College of Engineering, King Saud University, P.O. Box 800, Riyadh 11421, Saudi ArabiaPresident Office, King Abdulaziz City for Science and Technology (KACST), P.O. Box 6086, Riyadh 11442, Saudi ArabiaThe rhodium oxide (Rh<sub>2</sub>O<sub>3</sub>) doping effect on the activity and stability of nickel catalysts supported over yttria-stabilized zirconia was examined in dry reforming of methane (DRM) by using a tubular reactor, operated at 800 °C. The catalysts were characterized by using several techniques including nitrogen physisorption, X-ray diffraction, transmission electron microscopy, H<sub>2</sub>-temperature programmed reduction, CO<sub>2</sub>-temperature programmed Desorption, and temperature gravimetric analysis (TGA). The morphology of Ni-YZr was not affected by the addition of Rh<sub>2</sub>O<sub>3</sub>. However, it facilitated the activation of the catalysts and reduced the catalyst’s surface basicity. The addition of 4.0 wt.% Rh<sub>2</sub>O<sub>3</sub> gave the optimum conversions of CH<sub>4</sub> and CO<sub>2</sub> of ~89% and ~92%, respectively. Furthermore, the incorporation of Rh<sub>2</sub>O<sub>3</sub>, in the range of 0.0–4.0 wt.% loading, enhanced DRM and decreased the impact of reverse water gas shift, as inferred by the thermodynamics analysis. TGA revealed that the addition of Rh<sub>2</sub>O<sub>3</sub> diminished the carbon formation on the spent catalysts, and hence, boosted the stability, owing to the potential of rhodium for carbon oxidation through gasification reactions. The 4.0 wt.% Rh<sub>2</sub>O<sub>3</sub> loading gave a 12.5% weight loss of carbon. The TEM images displayed filamentous carbon, confirming the TGA results.https://www.mdpi.com/2079-4991/13/3/547methane dry reformingyttria-stabilized zirconia supportnickel-based catalystRh<sub>2</sub>O<sub>3</sub> promoterTGA results |
spellingShingle | Jehad Saleh Ahmed Sadeq Al-Fatesh Ahmed Aidid Ibrahim Francesco Frusteri Ahmed Elhag Abasaeed Anis Hamza Fakeeha Fahad Albaqi Khalid Anojaidi Salwa B. Alreshaidan Ibrahim Albinali Abdulrahman A. Al-Rabiah Abdulaziz Bagabas Stability and Activity of Rhodium Promoted Nickel-Based Catalysts in Dry Reforming of Methane Nanomaterials methane dry reforming yttria-stabilized zirconia support nickel-based catalyst Rh<sub>2</sub>O<sub>3</sub> promoter TGA results |
title | Stability and Activity of Rhodium Promoted Nickel-Based Catalysts in Dry Reforming of Methane |
title_full | Stability and Activity of Rhodium Promoted Nickel-Based Catalysts in Dry Reforming of Methane |
title_fullStr | Stability and Activity of Rhodium Promoted Nickel-Based Catalysts in Dry Reforming of Methane |
title_full_unstemmed | Stability and Activity of Rhodium Promoted Nickel-Based Catalysts in Dry Reforming of Methane |
title_short | Stability and Activity of Rhodium Promoted Nickel-Based Catalysts in Dry Reforming of Methane |
title_sort | stability and activity of rhodium promoted nickel based catalysts in dry reforming of methane |
topic | methane dry reforming yttria-stabilized zirconia support nickel-based catalyst Rh<sub>2</sub>O<sub>3</sub> promoter TGA results |
url | https://www.mdpi.com/2079-4991/13/3/547 |
work_keys_str_mv | AT jehadsaleh stabilityandactivityofrhodiumpromotednickelbasedcatalystsindryreformingofmethane AT ahmedsadeqalfatesh stabilityandactivityofrhodiumpromotednickelbasedcatalystsindryreformingofmethane AT ahmedaididibrahim stabilityandactivityofrhodiumpromotednickelbasedcatalystsindryreformingofmethane AT francescofrusteri stabilityandactivityofrhodiumpromotednickelbasedcatalystsindryreformingofmethane AT ahmedelhagabasaeed stabilityandactivityofrhodiumpromotednickelbasedcatalystsindryreformingofmethane AT anishamzafakeeha stabilityandactivityofrhodiumpromotednickelbasedcatalystsindryreformingofmethane AT fahadalbaqi stabilityandactivityofrhodiumpromotednickelbasedcatalystsindryreformingofmethane AT khalidanojaidi stabilityandactivityofrhodiumpromotednickelbasedcatalystsindryreformingofmethane AT salwabalreshaidan stabilityandactivityofrhodiumpromotednickelbasedcatalystsindryreformingofmethane AT ibrahimalbinali stabilityandactivityofrhodiumpromotednickelbasedcatalystsindryreformingofmethane AT abdulrahmanaalrabiah stabilityandactivityofrhodiumpromotednickelbasedcatalystsindryreformingofmethane AT abdulazizbagabas stabilityandactivityofrhodiumpromotednickelbasedcatalystsindryreformingofmethane |