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1000 MW超超临界锅炉热效率正平衡和反平衡模型分析 被引量:9
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作者 张继东 陈笔 +4 位作者 赵思嘉 周健 兰俊生 戴成峰 赵俊杰 《锅炉技术》 北大核心 2019年第2期21-26,共6页
建立1 000 MW超超临界机组锅炉热效率的正平衡和反平衡计算模型,定量分析负荷和过量空气系数等因素对锅炉实际热效率的影响规律。结果表明:平衡模型相比正平衡模型更适用于非稳态工况的锅炉热效率实时计算。本案例的实际锅炉热效率低于... 建立1 000 MW超超临界机组锅炉热效率的正平衡和反平衡计算模型,定量分析负荷和过量空气系数等因素对锅炉实际热效率的影响规律。结果表明:平衡模型相比正平衡模型更适用于非稳态工况的锅炉热效率实时计算。本案例的实际锅炉热效率低于设计值,且在高负荷下较大偏离设计值。实际锅炉热效率随负荷增加先增大后减小,在负荷680 MW时取得极大值。在高负荷下排烟温度和剩余氧气体积百分含量均远高于设计值,导致排烟热损失增大。合理降低高负荷下的剩余氧气体积百分含量和排烟温度,能提高锅炉热效率。 展开更多
关键词 锅炉热效率 排烟热损失 过量空气系数 平衡模型 反平衡模型
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Methodology for Design of Reactive Distillation Column and Kinetics for Isoamylene Etherification Catalysed by Amberlyst 35 被引量:1
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作者 Wu Yanli Li Wenying +1 位作者 Li Qiang Feng Jie 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2016年第4期128-136,共9页
Isoamylene from the Fischer-Tropsch syncrude can be transformed to valuable fuel oxygenate additives through an equilibrium limited etherification reaction with methanol. A reactive distillation process is established... Isoamylene from the Fischer-Tropsch syncrude can be transformed to valuable fuel oxygenate additives through an equilibrium limited etherification reaction with methanol. A reactive distillation process is established to increase isoamylene conversion. Facing the challenge of improving product purity at the same time, an equilibrium stage model based design methodology is proposed and illustrated step-by-step for converting the Fischer-Tropsch C_5 olefins to tert-amyl methyl ether(TAME) process by using Aspen Plus. Under the guide of the proposed methodology, the design leads to a TAME product purity of higher than 95% and an isoamylene conversion of higher than 90%. The etherification kinetics over Amberlyst 35 is also studied within a temperature range of 60 ℃ to 75 ℃ to shed more light on the feasibility of process development. The methodology provides an effective reactive distillation column design to achieve the target reactant conversion and product purity simultaneously. 展开更多
关键词 Amberlyst 35 design methodology etherification isoamylene reactive distillation column
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