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Performance analysis of a novel low CO2-emission solar hybrid combined cycle power system

机译:新型低二氧化碳排放的太阳能混合联合循环发电系统的性能分析

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This paper is a proposal and analysis of a novel low-CO2 emission solar hybrid combined cycle power system, which is based on solar-driven methane reforming. Nearly full methane conversion is achieved at a mild temperature (similar to 550 degrees C) using a methane reforming reactor integrated with a hydrogen separation membrane, enabling the solar thermal energy collected at middle temperature to be applied as the reaction heat in methane reforming, thereby converting the solar heat to chemical energy of the produced syngas. The membrane reactor also offers the advantage of continuously withdrawing hydrogen from the reaction zone, which is then burned at high temperature for power generation in the proposed advanced combined cycle system. The CO2-enriched gas concentrated at the end of the reaction zone is processed through pre-combustion decarbonization. It is shown that system thermal efficiency of 51.6% can be obtained, which is 2.2%-points higher than that of a referenced gas-steam combined cycle system with post-combustion decarbonization (CC-Post) at an equal CO2 removal ratio and no solar assistance. Fossil fuel saving ratio of 31.2% is achieved with a solar thermal share of 28.2%. Exergy analysis indicates that the main contributors for efficiency improvements are the reduced exergy destructions in the combustion and CO2 separation processes. The hybrid system has an exergy efficiency of 58% with 91% CO2 capture, which is 10%-points higher than that of a comparable CC-Post system. A preliminary economic analysis predicts that levelized electricity cost and payback period for the system are found to be 0.062 $/kWh and 10 years, respectively, and cost of CO2 avoided is 81 $/(ton CO2), which is 42.5% lower than that for a CC-Post system. The proposed system hybridization approach simultaneously achieves the dual-purpose of high-efficiency solar heat conversion and low-energy penalty CO2 capture. (C) 2017 Elsevier Ltd. All rights reserved.
机译:本文是对基于太阳能驱动的甲烷重整的新型低CO2排放太阳能混合联合循环发电系统的建议和分析。使用集成有氢分离膜的甲烷重整反应器,在温和的温度(大约550摄氏度)下,几乎可以实现甲烷的完全转化,从而使在中间温度收集的太阳能能用作甲烷重整中的反应热,从而将太阳热转化为产生的合成气的化学能。膜反应器还具有从反应区连续抽出氢气的优势,然后在提出的先进联合循环系统中将其在高温下燃烧发电。通过预燃烧脱碳处理浓缩在反应区末端的富集CO2的气体。结果表明,在相同的CO2去除率且无二氧化碳的情况下,可获得的系统热效率为51.6%,比具有后燃烧脱碳(CC-Post)的参比燃气-蒸汽联合循环系统的热效率高2.2%。太阳能援助。化石燃料节省率为31.2%,太阳能热份额为28.2%。火用分析表明,提高效率的主要因素是减少了燃烧和二氧化碳分离过程中的火用破坏。混合系统的能效效率为58%,二氧化碳捕集率为91%,比同类CC-Post系统高出10%。初步的经济分析预测,该系统的平均电力成本和投资回收期分别为0.062美元/千瓦时和10年,避免的CO2成本为81美元/(吨CO2),比成本降低42.5%。用于CC-Post系统。所提出的系统混合方法同时实现了高效太阳能热转换和低能耗二氧化碳捕获的双重目的。 (C)2017 Elsevier Ltd.保留所有权利。

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