Abst'/> So1ar Rankine Cycle (SRC) powered by Linear Fresnel solar field and integrated with Multi Effect Desalination (MED) system
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So1ar Rankine Cycle (SRC) powered by Linear Fresnel solar field and integrated with Multi Effect Desalination (MED) system

机译:由线性菲涅尔太阳能场供电并与多效脱盐(MED)系统集成的太阳能朗肯循环(SRC)

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摘要

AbstractThe Linear Fresnel (LF) solar filed was considered to support part of the required thermal energy of the Solar Rankin Cycle (SRC). Multi Effect Desalination (MED) system was applied in order to produce distillate water by using the SRC thermal energy. Two typical low temperature MED systems with 14 effects and two Gain Output Ratios (GORs) of 9.8 and 12 were considered to be feed by the steam (70 °C) at the outlet of the turbine replacing the condenser of SRC. Two thermal storage capacities of 6 and 12 h were considered in SRC calculations. Two LF solar fields were considered to operate with different mass flow rates and aperture areas. An economic analysis was also used to determine the water and electricity costs of the SRC/MED plant. The electricity unit cost of the SRC/MED plant was compared to electricity cost of a reference SRC plant (SRC/Ref) without MED and comprising a once-through cooling condenser with cooling temperature of 35 °C. The amount of annual fuel saving and the unit cost of the water and electricity were determined under different scenarios of MED unit GORs and for two thermal storage capacities.HighlightsA low part of required thermal energy of MED is supported by using Linear Fresnel field without thermal storage.SRC/MED/LF system with higher GORs has lower water production costs.The amount of annual fuel consumption would be considerably decreased by using the LF solar field.Minimum LCOE is obtained at a same solar multiple for two different GOR values.The water production cost is most sensitive to the solar field costs.
机译: 摘要 线性菲涅尔(LF)太阳能被认为可以支持太阳能Rankin循环(SRC)所需的部分热能。为了利用SRC热能生产蒸馏水,应用了多效脱盐(MED)系统。两种具有14种效果,两种增益输出比(GOR)为9.8和12的典型低温MED系统被认为是由涡轮机出口处的蒸汽(70°C)代替了SRC冷凝器供给的。在SRC计算中考虑了两个6h和12h的蓄热能力。考虑了两个低频太阳场以不同的质量流率和孔径面积工作。还使用了经济分析来确定SRC / MED工厂的水电成本。将SRC / MED工厂的电力成本与没有MED且包括冷却温度为35°C的直通式冷却冷凝器的参考SRC工厂(SRC / Ref)的电力成本进行了比较。在MED单位GOR的不同情况下以及两个蓄热能力下,确定了每年的燃料节省量和水电成本。 突出显示 < ce:label>• 使用线性菲涅耳字段而不存储热量,即可满足MED所需的少量热能。 SRC具有较高GOR的/ MED / LF系统具有较低的水生产成本。 通过使用LF太阳场,每年的燃油消耗量将大大减少。 < ce:list-item id =“ u0025”> 在两个不同的太阳能倍数下,最小LCOE值相同GOR值。 水的生产成本对太阳能成本最为敏感。

著录项

  • 来源
    《Renewable energy》 |2018年第3期|52-70|共19页
  • 作者单位

    Department of Mechanical Engineering, Faculty of Engineering, Shahid Bahonar University of Kerman;

    Department of Mechanical Engineering, Faculty of Engineering, Shahid Bahonar University of Kerman,Energy and Environmental Engineering Research Center, Shahid Bahonar University of Kerman;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    MED; Linear Fresnel; Solar Rankine Cycle; Thermal storage; Natural gas fuel;

    机译:MED;线性菲涅耳;太阳能兰金循环;储热;天然气燃料;
  • 入库时间 2022-08-18 00:24:48

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