Steam Cracking : Kinetics and Feed Characterisation
Steam Cracking : Kinetics and Feed Characterisation
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蒸汽裂解:动力学和进料表征
DOI:
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发表时间:
2015
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影响因子:
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通讯作者:
J. Moreira
中科院分区:
文献类型:
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作者:
J. Moreira
In the present work a mathematical steam cracking furnace model is presented and several kinetic schemes from literature, both molecular and radical, were implemented and validated against data from industrial ethane, propane and naphtha feedstocks processing furnaces. The results showed that, for gaseous feedstocks, the implemented kinetics were able to accurately predict product yields, with the radical scheme superseding the molecular one. Regarding naphtha cracking, however, the implemented radical kinetics from literature seemed to fail at predicting plant data. A steady-state study on alternative diluents relatively to steam was also carried out and it was concluded that there may actually be no difference between diluents if one is not willing to further increase the coil outlet temperature, although helium posed the best alternative if no constraints on temperature exist. At last, since the implementation of kinetic schemes require the molecular composition of the feed and because liquid feedstocks are usually characterised by other indices rather than a detailed hydrocarbon analysis, a feed characterisation model was developed. This model had the objective to determine the molecular composition of naphtha feedstocks given the commercial indices that usually characterise such petroleum fractions. The results, however, showed that the model is not able to accurately determine such compositions, having been concluded that a priori knowledge had to be included to improve its predictions.