首页> 外文会议>ASME international conference on energy sustainability >EXPERIMENTAL TESTING OF S-CO2 REGENERATOR FOR USE AS A REPLACEMENT TO HIGH COST PRINTED CIRCUIT RECUPERATORS FOR USE IN S-CO2 RECOMPRESSION BRAYTON CYCLE
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EXPERIMENTAL TESTING OF S-CO2 REGENERATOR FOR USE AS A REPLACEMENT TO HIGH COST PRINTED CIRCUIT RECUPERATORS FOR USE IN S-CO2 RECOMPRESSION BRAYTON CYCLE

机译:用S-CO2蓄热器代替用于S-CO2压缩布雷顿循环的高成本印刷电路蓄热器的实验测试

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Supercritical Carbon Dioxide (sCO2) power cycles have the potential to deliver high efficiency at low cost. However, in order for S-CO2 cycle to reach high efficiency, highly effective recuperators are needed. These recuperative heat exchangers must transfer heat at a rate that is substantially larger than the heat transfer to the cycle itself and can therefore represent up to 24% of the total power block cost in a recompression Brayton cycle. Lower cost regenerators are proposed as a cost saving alternative to high cost printed circuit recuperators. A regenerator is a heat exchanger that alternately has hot and cold fluid passing through it. During the first half of its cycle the hot gas is passed over a storage media bed (stainless steel balls, screens, or similar fill material) where thermal energy is stored. During the next half of the cycle, cold fluid is passed through in the opposite direction, extracting the thermal energy from the bed. By operating a cycle with two (or more) regenerators, where one is always in a hot to cold (HTC) blow and the other in a cold to hot blow (CTH), a quasi-steady state can be achieved in the cycle to allow continuous operation. A model of the regenerator was created and used in place of a recuperator in a model of a 10MW power plant. The thermal effectiveness of the regenerator cycle was slightly lower than the recuperator cycle, however the regenerator cycle had a saving of about 9.3 percent in the Levelized Cost of Energy (LCoE). A scale model of the regenerator is under construction which will verify the performance of the regenerator model.
机译:超临界二氧化碳(sCO2)功率循环具有以低成本提供高效率的潜力。但是,为了使S-CO2循环达到高效,需要高效的换热器。这些同流换热器的传热速率必须比传递给循环本身的传热速率大得多,因此,在再压缩布雷顿循环中,它们最多可占总功率块成本的24%。提出了低成本的蓄热器,以替代高成本的印刷电路蓄热器。蓄热器是一种热交换器,交替地有热流体和冷流体通过该热交换器。在其循环的前半段中,热气会通过存储热能的存储介质床(不锈钢球,筛网或类似的填充材料)。在循环的下半部分,冷流体沿相反方向通过,从床中提取热能。通过使用两个(或多个)蓄热器运行一个循环,其中一个总是处于热至冷(HTC)吹气,而另一个处于冷至热吹(CTH)时,可以在循环中实现准稳态。允许连续运行。创建了蓄热器模型,并在10MW电厂模型中代替了蓄热器。蓄热循环的热效率略低于蓄热循环,但是蓄热循环的平均能源成本(LCoE)节省了约9.3%。正在构建再生器的比例模型,该模型将验证再生器模型的性能。

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