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反应精馏过程中的多稳态分析 总被引:3,自引:0,他引:3
Reactive distillation processes for synthesis of ethylene glycol (EG) and ethyl tert-butyl ether (ETBE) were modeled with the simulation package ASPEN PLUS. The input multiplicity and output multiplicity were discussed with the method of sensitivity analysis for both cases. In EG production process, steady state multiplicities were studied in terms of effective liquid holdup volume and boil-up ratio. In ETBE synthesis process, the user kinetic subroutine was supplied into ASPEN PLUS firstly, and then the composition, temperature and reaction-rate profiles within the reactive distillation column were presented in detail. A set of stable solution branches based on distinct initial guesses for a range of boil-up ratio were found in EG synthesis. Input multiplicities were observed for a range of reboiler duty at several values of reflux ratio for ETBE synthesis process. These results can be used to avoid excessive energy consumption and achieve optimum design of reactive distillation column. 相似文献
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控制电力生产过程中NOx生成量的方法主要是分级燃烧.选择国内具有代表性的300 MW燃煤电站锅炉为对象,对锅炉不进行改造,在不同负荷条件下,利用分级燃烧原理,通过炉内优化分级燃烧试验,得出了降低炉内NOx生成的控制参数.额定负荷时,炉内NOx排放浓度在原有基础上降低了22.45%,有效地控制了NOx的排放. 相似文献
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