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Recovery of hydrogen from coke - oven gas by forming hydrate / Qiang Sun in Industrial & engineering chemistry research, Vol. 51 N° 17 (Mai 2012) 

Public ISBD [article]  in Industrial & engineering chemistry research > Vol. 51 N° 17 (Mai 2012) . - pp. 6205-6211 Titre : Recovery of hydrogen from coke - oven gas by forming hydrate Type de document : texte imprimé Auteurs : Qiang Sun, Auteur ; Jiangjie Dong, Auteur ; Xuqiang Guo, Auteur Année de publication : 2012 Article en page(s) : pp. 6205-6211 Note générale : Industrial chemistry Langues : Anglais (eng) Mots-clés : Coke  oven  gas Résumé : Coke-oven gas (COG), a byproduct of the coking process, has a relatively large fraction of hydrogen (H2). However, most COG is combusted away directly, resulting in serious waste of resources. Taking advantage of a separation gas mixture containing H2, we used a hydrate separation method in this work to recover H2 from COG. The formation conditions of COG hydrate were measured in 6 mol % tetrahydrofuran (THF) solution, which could significantly reduce COG hydrate formation pressures and make it possible to realize the industrial application of the separation technology. On this basis, the separation experiments were conducted in THF solution and THF-sodium dodecyl sulfate (SDS) solution, respectively. The experimental results of two-stage separation of COG via hydrate formation were obtained, and the effects of SDS on the reaction velocity were investigated as well. The results show that after one-stage separation, the content of H2 in residual gas can be increased from 48.41 mol % to about 65 mol %, and the recovery of H2 ranges from 81% to 96%. After two-stage separation, the content of H2 in residual gas ranges from 76 mol % to 84 mol %, and the recovery of H2 is between 72% and 91%. With the presence of SDS, the hydration reaction velocity is sped up to some extent, and the induction time and reaction time of hydrate formation are greatly shortened. ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie203041n [article] Recovery of hydrogen from coke - oven gas by forming hydrate [texte imprimé] / Qiang Sun, Auteur ; Jiangjie Dong, Auteur ; Xuqiang Guo, Auteur . - 2012 . - pp. 6205-6211. Industrial chemistry Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 51 N° 17 (Mai 2012) . - pp. 6205-6211 Mots-clés : Coke  oven  gas Résumé : Coke-oven gas (COG), a byproduct of the coking process, has a relatively large fraction of hydrogen (H2). However, most COG is combusted away directly, resulting in serious waste of resources. Taking advantage of a separation gas mixture containing H2, we used a hydrate separation method in this work to recover H2 from COG. The formation conditions of COG hydrate were measured in 6 mol % tetrahydrofuran (THF) solution, which could significantly reduce COG hydrate formation pressures and make it possible to realize the industrial application of the separation technology. On this basis, the separation experiments were conducted in THF solution and THF-sodium dodecyl sulfate (SDS) solution, respectively. The experimental results of two-stage separation of COG via hydrate formation were obtained, and the effects of SDS on the reaction velocity were investigated as well. The results show that after one-stage separation, the content of H2 in residual gas can be increased from 48.41 mol % to about 65 mol %, and the recovery of H2 ranges from 81% to 96%. After two-stage separation, the content of H2 in residual gas ranges from 76 mol % to 84 mol %, and the recovery of H2 is between 72% and 91%. With the presence of SDS, the hydration reaction velocity is sped up to some extent, and the induction time and reaction time of hydrate formation are greatly shortened. ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie203041n