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首页> 外文期刊>Energy Conversion & Management >Transient simulation of a solar heating system for a small-scale ethanol-water distillation plant: Thermal, environmental and economic performance
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Transient simulation of a solar heating system for a small-scale ethanol-water distillation plant: Thermal, environmental and economic performance

机译:小型乙醇-水蒸馏厂的太阳能加热系统的瞬态模拟:热,环境和经济绩效

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The thermal, environmental and economic performance of a small-scale ethanol distillation system, where solar energy is used as primary energy source, was studied. Two different concentrations of ethanol at the feed stream (5 wt.% and 10 wt.%) were analysed to obtain a distillate product of 95 wt.% ethanol (hydrous ethanol). Evacuated tube solar collectors (ETC) and parabolic trough collectors (PTC) were considered for the solar heating system. A case of study for a specific geographical place (Monterrey, Mexico) was developed herein to evaluate the solar ethanol distillation system; the results can be extended to other locations, weather conditions and operational parameters. The thermal results from the simulation showed that through an adequate selection of the solar collector area and an appropriate sizing of the different equipment of the solar distillation system, PTC represents a better option where energy savings of 80% and 71% can be achieved for 5 wt.% and 10 wt.% ethanol at the feed stream, respectively. However, the economic feasibility of the solar distillation system is achieved using ETC for a price of hydrous ethanol of 1.75 USD/L and a feed stream of 10 wt.% ethanol, reaching an internal rate of return (IRR) of 18.8% and payback period of 5.2 years. As an important technical result, selected ETC presented advantages over PTC where an average distillate product of 3.6 and 3.4 ml at 95 wt.% ethanol can be obtained per unit of solar energy (kW h) captured per area (m(2)) of solar collector using 5 wt.% and 10 wt.% ethanol at the feed stream, respectively (36% more than PTC). The reduction of greenhouse gases (GHG) was of 72.4 kg CO2/yr per area (m(2)) for evacuated tube solar collector (at least 8% more than PTC). These results are considered useful as they would provide valuable information to members of the ethanol distillation industry, the fuel industry, policy makers in renewable energy, and installers. (C) 2016 Elsevier Ltd. All rights reserved.
机译:研究了以乙醇为主要能源的小型乙醇蒸馏系统的热,环境和经济性能。分析进料流中两种不同浓度的乙醇(5重量%和10重量%)以获得95重量%乙醇(含水乙醇)的馏出产物。太阳能加热系统考虑了真空管式太阳能集热器(ETC)和抛物线槽式集热器(PTC)。本文开发了一个针对特定地理位置(墨西哥蒙特雷)的研究案例,以评估太阳能乙醇蒸馏系统。结果可以扩展到其他位置,天气条件和操作参数。模拟的热结果表明,通过适当选择太阳能集热器区域并适当调整太阳能蒸馏系统的不同设备的尺寸,PTC代表了更好的选择,其中对于5台而言,可以节省80%和71%的能源进料流中的乙醇分别为10重量%和10重量%。但是,使用ETC以1.75美元/升的含水乙醇价格和10 wt。%的乙醇进料流实现太阳能蒸馏系统的经济可行性,内部收益率(IRR)为18.8%,投资回收期期限为5.2年。作为一项重要的技术成果,选定的ETC优于PTC,在PTC上每单位面积(m(2))所捕获的每单位太阳能(kW h)可获得3.6和3.4 ml的乙醇(重量百分比为95)的平均馏出物。太阳能收集器在进料流处分别使用5 wt。%和10 wt。%的乙醇(比PTC多36%)。真空管式太阳能集热器的温室气体(GHG)减少量为每区域72.4 kg CO2 / yr(m(2))(比PTC多至少8%)。这些结果被认为是有用的,因为它们将为乙醇蒸馏行业的成员,燃料行业,可再生能源的政策制定者以及安装人员提供有价值的信息。 (C)2016 Elsevier Ltd.保留所有权利。

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