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Thermo-economic Performance Analysis Of Kalina Cycle Based On Low Temperature Flue Gas Waste Heat Power Generation

Posted on:2018-10-01Degree:MasterType:Thesis
Country:ChinaCandidate:F WangFull Text:PDF
GTID:2322330533461671Subject:Master of Engineering
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This project mainly focused on analysed the thermo-economic performance of the Kalina cycle driven by the low temperature flue gas waste heat.Taking the Kalina cycle as the research object,the thermo-economic performance versus outlet temperature of flue gas were analyzed under variations of the pinch point temperature difference of evaporator??Te?,evaporation pressure?pe?and basic ammonia mass fraction?x?.Considering the corrosion of low temperature flue gas,the necessity and reasonability of limiting outlet temperature of flue gas at its minimum allowed discharge temperature were studied.Moreover,considering the thermodynamic and economic constraints simultaneously,the critical external heat source conditions available for Kalina syste m are clarified.The critical external heat source conditions include the maximum allowed heat source temperature Tgi,max,the minimum allowed heat source temperature Tgi,min and the minimum allowed heat source mass flow rate mg,min.Results show that the system exists optimal outlet temperature of flue gas(Tgo,opt)and evaporation pressure(pe,opt)for levelized energy cost?LEC?,while the optimal outlet temperature of flue gas(Tgo,opt)is associated with the pinch point temperature difference of evaporator?? Te?,evaporation pressure?pe?and basic ammonia mass fraction?x?.For net work?Wnet?and exergy efficiency??e x?,it only exists optimal evaporation pressure(pe,opt).The economic factors affect directly the optimal operation parameters of the system.The economic factors and low temperature flue gas corrosion problem should be considered comprehensively to choose the appropriate operation parameters in view of different heat source conditions.In addition,the maximum allowed heat source temperature Tgi,max and the minimum allowed heat source temperature Tgi,min gradually decrease with the increasing of ammonia mass fraction under the fixed evaporating pressure pe.And the greater the ammonia mass fraction,the narrower the temperature range of heat source that can be used.The flue gas mass flow rate mg has significant impact on the minimum allowed heat source temperature Tgi,min.Along with the flue gas mass flow rate mg increases,the minimum allowed heat source temperature Tgi,min becomes lower.When the ammonia mass fraction is in a certain condition,the maximum allowed heat source temperature Tgi,max increases with the increasing of the evaporating pressure pe while the minimum allowed heat source temperature Tgi,min and the minimum allowed heat source mass flow rate mg,min firstly fall down,then rise up with the increasing of evaporating pressure pe.And the minimum allowed heat source mass flow rate mg,min reduces sharply with the increase of heat source temperature Tgi.For the comparative between Kalina cycle and sub-ORC under different heat source conditions,the appropriate zeotropic mixtures and ammonia ratio were selected based on performance optimization in the first place,then compared the thermo-economic performance between the Kalina cycle and subcritical organic Rankine cycle.The results show that,the distribution ratio of the working fluids doesn't exist when the thermodynamic performance and economic performance of the the subcritical ORC cycle system are both optimal.When LEC is used as the economic evaluation index,the economic performance of the pure refrigerant is better than that of the zeotropic mixtures;but the thermal performance of the pure refrigerant is worse than that of the zeotropic mixtures when choose Wnet as the thermal evaluation index.In the range of Tgo,the thermal performance of subcritical ORC cycle is better than that of Kalina cycle,and the Kalina cycle economic performance is bet ter than that of ORC.The highest proportion of exergy loss of Kalina cycle and subcritical ORC cycle is the condenser and evaporator,the turbine is the second,so as for the optimization of syste m components,evaporator,condenser and turbine are the key to the improve Kalina cycle and subcritical ORC.In the range of Tgi,there exists critical Tgi(Tgi,cr).If Tgi is higher than Tgi,cr,the thermal performance of the subcritical ORC cycle is prior,on the contrary,the Kalina cycle is preferential.But the economic performance of Kalina cycle is always better than that of subcritical ORC cycle.
Keywords/Search Tags:waste heat power generation, Kalina cycle, subcritical organic Rankine cycle, critical heat source condition, thermo-economic performance
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