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改善KR搅拌脱硫混合特性的理论分析与实践 被引量:11
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作者 欧阳德刚 邹继新 +3 位作者 蒋扬虎 朱善合 李明晖 罗巍 《武钢技术》 CAS 2011年第5期14-18,共5页
通过KR搅拌脱硫流动状态分析,探明了其局域卷吸混合分散特性;根据固体回转部半径rc与搅拌器叶轮半径r1间的经验公式与搅拌功率影响因素,探讨了改善KR搅拌脱硫混合特性(动力学条件)的具体措施;通过对国内外不同结构搅拌器的工业性试验与... 通过KR搅拌脱硫流动状态分析,探明了其局域卷吸混合分散特性;根据固体回转部半径rc与搅拌器叶轮半径r1间的经验公式与搅拌功率影响因素,探讨了改善KR搅拌脱硫混合特性(动力学条件)的具体措施;通过对国内外不同结构搅拌器的工业性试验与应用研究结果的分析,证实了改善措施的理论研究结果对实际生产良好的指导价值。 展开更多
关键词 铁水脱硫 机械搅拌 流态 混合分散 反应动力学条件
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Removal of diclofenac from aqueous solution with multi-walled carbon nanotubes modified by nitric acid 被引量:3
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作者 胡翔 程昭 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2015年第9期1551-1556,共6页
Modified multi-walled carbon nanotubes(MWCNTs) were used as adsorbents for removal of diclofenac. The reaction conditions were examined. Langmuir, Freundlich, Temkin, and Dubinin–Radushkevich isotherm models were app... Modified multi-walled carbon nanotubes(MWCNTs) were used as adsorbents for removal of diclofenac. The reaction conditions were examined. Langmuir, Freundlich, Temkin, and Dubinin–Radushkevich isotherm models were applied to determine appropriate equilibrium expression. The results show that the experimental data fit the Freundlich equation well. Thermodynamic parameters show that the adsorption process is spontaneous and exothermic. The kinetic study indicates that the adsorption of diclofenac can be well described with the pseudo-second-order kinetic model and the process is controlled by multiple steps. 展开更多
关键词 Diclofenac Multi-walled carbon nanotubes Adsorption Isotherm equilibrium Thermodynamic Kinetic modeling
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Interpreting the dynamic effect of internal heat integration on reactive distillation columns
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作者 Yang Yuan Liang Zhang +3 位作者 Haisheng Chen Shaofeng Wang Kejin Huang Huan Shao 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2017年第1期89-102,共14页
In this work,the impact of internal heat integration upon process dynamics and controllability by superposing reactive section onto stripping section,relocating feed locations,and redistributing catalyst within the re... In this work,the impact of internal heat integration upon process dynamics and controllability by superposing reactive section onto stripping section,relocating feed locations,and redistributing catalyst within the reactive section is explored based on a hypothetical ideal reactive distillation system containing an exothermic reaction:A + BC + D.Steady state operation analysis and closed-loop controllability evaluation are carried out by comparing the process designs with and without the consideration of internal heat integration.For superposing reactive section onto stripping section,favorable effect is aroused due to its low sensitivities to the changes in operating condition.For ascending the lower feed stage,somewhat detrimental effect occurs because of the accompanied adverse internal heat integration and strong sensitivity to the changes in operating condition.For descending the upper feed stage,serious detrimental effect happens because of the introduced adverse internal heat integration and strong sensitivity to the changes in operating condition.For redistributing catalyst in the reactive section,fairly small negative influence is aroused by the sensitivity to the changes in operating condition.When reinforcing internal heat integration with a combinatorial use of these three strategies,the decent of the upper feed stage should be avoided in process development.Although the conclusions are derived based on the hypothetical ideal reactive distillation column studied,they are considered to be of general significance to the design and operation of other reactive distillation columns. 展开更多
关键词 Reactive distillation column Internal heat integration Process design Process dynamics Process control
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