Knowledge Management System Of Institute of process engineering,CAS
| simulationofoxyleneoxidationinfixedbedreactorusing1dheterogeneousmodel | |
| Hong Ruoyu1; Yang Wei2; Zhuang Yingqiang2; Li Hongzhong3 | |
| 2006 | |
| Source Publication | 计算机与应用化学
 |
| ISSN | 1001-4160 |
| Volume | 23Issue:6Pages:481 |
| Abstract | The oxidation of o-xylene to phthalic anhydride in a fixed-bed catalytic reactor was simulated using a one-dimensional （1-D） heterogeneous-phase model. The mass diffusion inside and outside catalyst pellets was taken into consideration. The gas-phase governing equations were solved using the fourth-order Runge-Kutta integration with adjustable steps. The solid-phase governing equations were solved using the shooting-method. The numerical results computed using the 1-D heterogeneous-phase model was compared with those using a 1-D pseudo-homogeneous-phase model and 2-D pseudo-homogeneous and heterogeneous-phase models Three correlation equations for predicting pressure drop reported in reference were compared and the best one was found. |
| Language | 英语 |
| Document Type | 期刊论文 |
| Identifier | http://ir.ipe.ac.cn/handle/122111/34319 |
| Collection | 中国科学院过程工程研究所 |
| Affiliation | 1.Soochow University,Department of Chemical Engineering 2.苏州大学 3.中国科学院过程工程研究所 |
| Recommended Citation GB/T 7714 | Hong Ruoyu,Yang Wei,Zhuang Yingqiang,et al. simulationofoxyleneoxidationinfixedbedreactorusing1dheterogeneousmodel[J]. 计算机与应用化学,2006,23(6):481. |
| APA | Hong Ruoyu,Yang Wei,Zhuang Yingqiang,&Li Hongzhong.(2006).simulationofoxyleneoxidationinfixedbedreactorusing1dheterogeneousmodel.计算机与应用化学,23(6),481. |
| MLA | Hong Ruoyu,et al."simulationofoxyleneoxidationinfixedbedreactorusing1dheterogeneousmodel".计算机与应用化学 23.6(2006):481. |
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