The utilisation of the C4 streams of steamcrackers by converting raffinate II to maleic anhydride was studied. The oxidation reactions were investigated in a laboratory-scale fixed-bed reactor to determine reaction kinetics. The effects of pore diffusional resistance were investigated and explained. A two-dimensional pseudo-homogeneous reactor model was used for the simulation of a production-scale fixed-bed reactor. A flow scheme of the reactor section including a recycle was proposed.
Umfang: VI, 186 S.
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Brandstädter, W. 2008. Partial oxidation of Raffinate II and other mixtures of n-Butane and n-Butenes to maleic anhydride in a fixed-bed reactor. Karlsruhe: KIT Scientific Publishing. DOI: https://doi.org/10.5445/KSP/1000007336
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Veröffentlicht am 4. Februar 2008
Englisch
199
Paperback | 978-3-86644-199-6 |