Hydrogen production by glycerol dry reforming over rhenium promoted Ni-based catalyst supported on Santa Barbara Amorphous 15 (SBA-15)
This paper presents the glycerol dry reforming (GDR) reaction using rhenium (Re) promoted on Ni-based catalyst supported on Santa Barbara Amorphous 15 (SBA-15) for the production of hydrogen. In this study, the non-promoted (15%Ni/SBA-15) and promoted (3%Re-15%Ni/SBA-15) catalysts were first synthes...
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| Format: | Article |
| Language: | English |
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Taylor & Francis
2019
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| Online Access: | http://umpir.ump.edu.my/id/eprint/26213/1/Hydrogen%20production%20by%20glycerol%20dry%20reforming%20over%20rhenium1.pdf |
| _version_ | 1825812936723005440 |
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| author | Nurul Asmawati, Roslan Nur Nabillah, Mohd Arif Jessy, Lynn Jaspin Nurul Aini, Mohamed Razali Sumaiya, Zainal Abidin |
| author_facet | Nurul Asmawati, Roslan Nur Nabillah, Mohd Arif Jessy, Lynn Jaspin Nurul Aini, Mohamed Razali Sumaiya, Zainal Abidin |
| author_sort | Nurul Asmawati, Roslan |
| collection | UMP |
| description | This paper presents the glycerol dry reforming (GDR) reaction using rhenium (Re) promoted on Ni-based catalyst supported on Santa Barbara Amorphous 15 (SBA-15) for the production of hydrogen. In this study, the non-promoted (15%Ni/SBA-15) and promoted (3%Re-15%Ni/SBA-15) catalysts were first synthesized using wet impregnation method and their physicochemical characteristics were analyzed with Brunauer–Emmet–Teller (BET), scanning electron microscopy (SEM), X-ray diffraction (XRD), and thermogravimetric (TGA) analyses. Their performances were evaluated in GDR reaction and it was found that 3%Re-15%Ni/SBA-15 exhibited higher glycerol conversion (57%) and hydrogen yield (55%) than 15%Ni/SBA-15 (i.e., 20% glycerol conversion and 18% hydrogen yield). From the GDR study, the highest glycerol conversion (57%) and hydrogen yield (55%) for 3%Re-15%Ni/SBA-15 were obtained at 0.2 g catalyst, 700°C of reaction temperature, and CO2 to glycerol ratio (CGR) of 1:1. The small crystallite size and BET surface area of 3%Re-15%Ni/SBA-15 had successfully reduced the carbon deposition and indirectly contributed to high glycerol conversion and product yield. |
| first_indexed | 2024-03-06T12:36:32Z |
| format | Article |
| id | UMPir26213 |
| institution | Universiti Malaysia Pahang |
| language | English |
| last_indexed | 2024-03-06T12:36:32Z |
| publishDate | 2019 |
| publisher | Taylor & Francis |
| record_format | dspace |
| spelling | UMPir262132019-10-30T03:29:54Z http://umpir.ump.edu.my/id/eprint/26213/ Hydrogen production by glycerol dry reforming over rhenium promoted Ni-based catalyst supported on Santa Barbara Amorphous 15 (SBA-15) Nurul Asmawati, Roslan Nur Nabillah, Mohd Arif Jessy, Lynn Jaspin Nurul Aini, Mohamed Razali Sumaiya, Zainal Abidin TP Chemical technology This paper presents the glycerol dry reforming (GDR) reaction using rhenium (Re) promoted on Ni-based catalyst supported on Santa Barbara Amorphous 15 (SBA-15) for the production of hydrogen. In this study, the non-promoted (15%Ni/SBA-15) and promoted (3%Re-15%Ni/SBA-15) catalysts were first synthesized using wet impregnation method and their physicochemical characteristics were analyzed with Brunauer–Emmet–Teller (BET), scanning electron microscopy (SEM), X-ray diffraction (XRD), and thermogravimetric (TGA) analyses. Their performances were evaluated in GDR reaction and it was found that 3%Re-15%Ni/SBA-15 exhibited higher glycerol conversion (57%) and hydrogen yield (55%) than 15%Ni/SBA-15 (i.e., 20% glycerol conversion and 18% hydrogen yield). From the GDR study, the highest glycerol conversion (57%) and hydrogen yield (55%) for 3%Re-15%Ni/SBA-15 were obtained at 0.2 g catalyst, 700°C of reaction temperature, and CO2 to glycerol ratio (CGR) of 1:1. The small crystallite size and BET surface area of 3%Re-15%Ni/SBA-15 had successfully reduced the carbon deposition and indirectly contributed to high glycerol conversion and product yield. Taylor & Francis 2019 Article PeerReviewed pdf en http://umpir.ump.edu.my/id/eprint/26213/1/Hydrogen%20production%20by%20glycerol%20dry%20reforming%20over%20rhenium1.pdf Nurul Asmawati, Roslan and Nur Nabillah, Mohd Arif and Jessy, Lynn Jaspin and Nurul Aini, Mohamed Razali and Sumaiya, Zainal Abidin (2019) Hydrogen production by glycerol dry reforming over rhenium promoted Ni-based catalyst supported on Santa Barbara Amorphous 15 (SBA-15). Energy Sources, Part A: Recovery, Utilization, and Environmental Effects. pp. 1-13. ISSN 1556-7036 (Print); 1556-7230 (Online). (In Press / Online First) (In Press / Online First) https://doi.org/10.1080/15567036.2019.1645762 https://doi.org/10.1080/15567036.2019.1645762 |
| spellingShingle | TP Chemical technology Nurul Asmawati, Roslan Nur Nabillah, Mohd Arif Jessy, Lynn Jaspin Nurul Aini, Mohamed Razali Sumaiya, Zainal Abidin Hydrogen production by glycerol dry reforming over rhenium promoted Ni-based catalyst supported on Santa Barbara Amorphous 15 (SBA-15) |
| title | Hydrogen production by glycerol dry reforming over rhenium promoted Ni-based catalyst supported on Santa Barbara Amorphous 15 (SBA-15) |
| title_full | Hydrogen production by glycerol dry reforming over rhenium promoted Ni-based catalyst supported on Santa Barbara Amorphous 15 (SBA-15) |
| title_fullStr | Hydrogen production by glycerol dry reforming over rhenium promoted Ni-based catalyst supported on Santa Barbara Amorphous 15 (SBA-15) |
| title_full_unstemmed | Hydrogen production by glycerol dry reforming over rhenium promoted Ni-based catalyst supported on Santa Barbara Amorphous 15 (SBA-15) |
| title_short | Hydrogen production by glycerol dry reforming over rhenium promoted Ni-based catalyst supported on Santa Barbara Amorphous 15 (SBA-15) |
| title_sort | hydrogen production by glycerol dry reforming over rhenium promoted ni based catalyst supported on santa barbara amorphous 15 sba 15 |
| topic | TP Chemical technology |
| url | http://umpir.ump.edu.my/id/eprint/26213/1/Hydrogen%20production%20by%20glycerol%20dry%20reforming%20over%20rhenium1.pdf |
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