Hydrogen production via sorption enhanced steam reforming of butanol: Thermodynamic analysis
β Scribed by Wenju Wang; Yingyu Cao
- Publisher
- Elsevier Science
- Year
- 2011
- Tongue
- English
- Weight
- 415 KB
- Volume
- 36
- Category
- Article
- ISSN
- 0360-3199
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β¦ Synopsis
Thermodynamic equilibrium for sorption enhanced steam reforming of butanol (SESRB) to hydrogen was investigated using Gibbs free energy minimization method. The optimal operation conditions for SESRB are at 800 K, the steam-to-butanol molar ratio of 10, the calcium oxide-to-butanol molar ratio of 8 and atmospheric pressure. Under the optimal conditions, complete conversion of butanol, 97.07% concentration of H 2 and 0.05% concentration of CO 2 , and efficiency of 86.60% could be achieved and at which no coke tends to form. Under the same conditions in SRB, 58.18% concentration of H 2 , 21.62% concentration of CO 2 , and energy efficiency of 81.51% could be achieved. Butanol steam reforming with CO 2 adsorption has the higher H 2 content and efficiency, and lower CO 2 content than that without adsorption under the same reaction conditions. In addition, reaction conditions for coke-free and coke-formed regions are also discussed in butanol steam reforming with or without CO 2 separation.
π SIMILAR VOLUMES
Thermodynamics was applied to investigate propane dry reforming (DR) and steam reforming (SR). Equilibrium calculations employing the Gibbs free energy minimization were performed upon a wide range of pressure (1e5 atm), temperature (700e1100 K), carbon dioxide to propane ratio (CPR, 1e12) and water