[article]
| Titre : |
A Natural Gas to Liquids Process Model for Optimal Operation |
| Type de document : |
texte imprimé |
| Auteurs : |
Mehdi Panahi, Auteur ; Ahmad Rafiee, Auteur ; Sigurd Skogestad, Auteur |
| Année de publication : |
2012 |
| Article en page(s) : |
pp. 425-433 |
| Note générale : |
Chimie industrielle |
| Langues : |
Anglais (eng) |
| Mots-clés : |
Modeling Natural gas |
| Résumé : |
The design and optimization of a natural gas to hydrocarbon liquids (GTL) process is considered, mainly from the view of maximizing the variable income during operation. Autothermal reforming (ATR) is used for synthesis gas production. The kinetic model for Fischer-Tropsch (FT) reactions is the one given by Iglesia et al. for a cobalt-based FT reactor. For the product distribution, three alternative expressions for the chain growth factor α are compared. |
| DEWEY : |
660 |
| ISSN : |
0888-5885 |
| En ligne : |
http://cat.inist.fr/?aModele=afficheN&cpsidt=25476486 |
in Industrial & engineering chemistry research > Vol. 51 N° 1 (Janvier 2012) . - pp. 425-433
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