Reaction kinetics of steam reforming of n-butanol over Ni/hydrotalcite catalyst

Abhimanyu K. Yadav, Prakash D. Vaidya
Wiley-Blackwell
Published 2018
Publication Date:
2018-02-07
Publisher:
Wiley-Blackwell
Print ISSN:
0930-7516
Electronic ISSN:
1521-4125
Topics:
Chemistry and Pharmacology
Process Engineering, Biotechnology, Nutrition Technology
Published by:
_version_ 1836398780734242816
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