Reaction kinetics of steam reforming of n-butanol over Ni/hydrotalcite catalyst
Publication Date: |
2018-02-07
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Publisher: |
Wiley-Blackwell
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Print ISSN: |
0930-7516
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Electronic ISSN: |
1521-4125
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Topics: |
Chemistry and Pharmacology
Process Engineering, Biotechnology, Nutrition Technology
|
Published by: |
_version_ | 1836398780734242816 |
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autor | Abhimanyu K. Yadav, Prakash D. Vaidya |
beschreibung | Bio-oil is a candidate renewable feedstock for hydrogen (H 2 ) production. In this work, n -butanol was chosen as a model compound representing alcohols in the bio-oil aqueous fraction. H 2 production from steam reforming of n -butanol was investigated in a fixed-bed reactor using commercial Ni/hydrotalcite catalyst. A plausible reaction pathway in presence of Ni was discussed. The rise in reforming temperature, space time and steam/carbon ratio in feed enhanced n -butanol conversion and H 2 yield. Reaction kinetics was studied in the chemical control regime (623-773 K). The reaction order with respect to n -butanol (one) and the activation energy (50 kJ/mol) were found. |
citation_standardnr | 6157122 |
datenlieferant | ipn_articles |
feed_id | 4519 |
feed_publisher | Wiley-Blackwell |
feed_publisher_url | http://www.wiley.com/wiley-blackwell |
insertion_date | 2018-02-07 |
journaleissn | 1521-4125 |
journalissn | 0930-7516 |
publikationsjahr_anzeige | 2018 |
publikationsjahr_facette | 2018 |
publikationsjahr_intervall | 7984:2015-2019 |
publikationsjahr_sort | 2018 |
publisher | Wiley-Blackwell |
quelle | Chemical Engineering and Technology |
relation | http://onlinelibrary.wiley.com/resolve/doi?DOI=10.1002%2Fceat.201600738 |
search_space | articles |
shingle_author_1 | Abhimanyu K. Yadav, Prakash D. Vaidya |
shingle_author_2 | Abhimanyu K. Yadav, Prakash D. Vaidya |
shingle_author_3 | Abhimanyu K. Yadav, Prakash D. Vaidya |
shingle_author_4 | Abhimanyu K. Yadav, Prakash D. Vaidya |
shingle_catch_all_1 | Reaction kinetics of steam reforming of n-butanol over Ni/hydrotalcite catalyst Bio-oil is a candidate renewable feedstock for hydrogen (H 2 ) production. In this work, n -butanol was chosen as a model compound representing alcohols in the bio-oil aqueous fraction. H 2 production from steam reforming of n -butanol was investigated in a fixed-bed reactor using commercial Ni/hydrotalcite catalyst. A plausible reaction pathway in presence of Ni was discussed. The rise in reforming temperature, space time and steam/carbon ratio in feed enhanced n -butanol conversion and H 2 yield. Reaction kinetics was studied in the chemical control regime (623-773 K). The reaction order with respect to n -butanol (one) and the activation energy (50 kJ/mol) were found. Abhimanyu K. Yadav, Prakash D. Vaidya Wiley-Blackwell 0930-7516 09307516 1521-4125 15214125 |
shingle_catch_all_2 | Reaction kinetics of steam reforming of n-butanol over Ni/hydrotalcite catalyst Bio-oil is a candidate renewable feedstock for hydrogen (H 2 ) production. In this work, n -butanol was chosen as a model compound representing alcohols in the bio-oil aqueous fraction. H 2 production from steam reforming of n -butanol was investigated in a fixed-bed reactor using commercial Ni/hydrotalcite catalyst. A plausible reaction pathway in presence of Ni was discussed. The rise in reforming temperature, space time and steam/carbon ratio in feed enhanced n -butanol conversion and H 2 yield. Reaction kinetics was studied in the chemical control regime (623-773 K). The reaction order with respect to n -butanol (one) and the activation energy (50 kJ/mol) were found. Abhimanyu K. Yadav, Prakash D. Vaidya Wiley-Blackwell 0930-7516 09307516 1521-4125 15214125 |
shingle_catch_all_3 | Reaction kinetics of steam reforming of n-butanol over Ni/hydrotalcite catalyst Bio-oil is a candidate renewable feedstock for hydrogen (H 2 ) production. In this work, n -butanol was chosen as a model compound representing alcohols in the bio-oil aqueous fraction. H 2 production from steam reforming of n -butanol was investigated in a fixed-bed reactor using commercial Ni/hydrotalcite catalyst. A plausible reaction pathway in presence of Ni was discussed. The rise in reforming temperature, space time and steam/carbon ratio in feed enhanced n -butanol conversion and H 2 yield. Reaction kinetics was studied in the chemical control regime (623-773 K). The reaction order with respect to n -butanol (one) and the activation energy (50 kJ/mol) were found. Abhimanyu K. Yadav, Prakash D. Vaidya Wiley-Blackwell 0930-7516 09307516 1521-4125 15214125 |
shingle_catch_all_4 | Reaction kinetics of steam reforming of n-butanol over Ni/hydrotalcite catalyst Bio-oil is a candidate renewable feedstock for hydrogen (H 2 ) production. In this work, n -butanol was chosen as a model compound representing alcohols in the bio-oil aqueous fraction. H 2 production from steam reforming of n -butanol was investigated in a fixed-bed reactor using commercial Ni/hydrotalcite catalyst. A plausible reaction pathway in presence of Ni was discussed. The rise in reforming temperature, space time and steam/carbon ratio in feed enhanced n -butanol conversion and H 2 yield. Reaction kinetics was studied in the chemical control regime (623-773 K). The reaction order with respect to n -butanol (one) and the activation energy (50 kJ/mol) were found. Abhimanyu K. Yadav, Prakash D. Vaidya Wiley-Blackwell 0930-7516 09307516 1521-4125 15214125 |
shingle_title_1 | Reaction kinetics of steam reforming of n-butanol over Ni/hydrotalcite catalyst |
shingle_title_2 | Reaction kinetics of steam reforming of n-butanol over Ni/hydrotalcite catalyst |
shingle_title_3 | Reaction kinetics of steam reforming of n-butanol over Ni/hydrotalcite catalyst |
shingle_title_4 | Reaction kinetics of steam reforming of n-butanol over Ni/hydrotalcite catalyst |
timestamp | 2025-06-30T23:32:31.464Z |
titel | Reaction kinetics of steam reforming of n-butanol over Ni/hydrotalcite catalyst |
titel_suche | Reaction kinetics of steam reforming of n-butanol over Ni/hydrotalcite catalyst |
topic | V ZM |
uid | ipn_articles_6157122 |