sCO2和ORC系统余热回收的技术经济比较

T. Allison, Jason C. Wilkes, Karl D. Wygant, Rob Pelton
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摘要

各种超临界二氧化碳(sCO2)动力循环是一种新兴的燃气轮机废热回收底循环技术,相对于有机朗肯循环(ORC)系统具有潜在的优势,包括改进的性能、紧凑性、改进的经济性、无危险的工作流体和更快的斜坡能力。这项工作比较了一个废热回收系统,该系统基于一个整体齿轮的compander,在sCO2预热循环配置中带有分裂的回热器和文献中的回热ORC。整体齿轮传动系统由一台1800转/分钟的发电机组成,高压和低压小齿轮将两级压缩机和膨胀器分开。描述了循环约束和设计驱动因素,以及sCO2系统的优化,以及目前的技术准备情况和各种组件(包括压缩机、膨胀器、热交换器和其他系统组件)的全压全温运行经验。两个循环都与商用15mw燃气轮机配对,并给出了由此产生的系统成本、性能和其他属性。在冷侧温度为35°C的条件下,循环结果显示ORC系统输出功率为5066 kW, sCO2系统输出功率为5660 kW,即sCO2性能提升11.7%。此外,还比较了基于sCO2和orc的系统的成本和尺寸要求以及成本,表明两种系统的名义成本相当,而sCO2系统的潜在成本更低,特别是当需要间接传热回路时。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Technoeconomic Comparison of sCO2 and ORC Systems for Waste Heat Recovery
Various supercritical carbon dioxide (sCO2) power cycles are an emerging bottoming cycle technology for gas turbine waste heat recovery with potential advantages relative to Organic Rankine Cycle (ORC) systems, including improved performance, compactness, improved economics, nonhazardous working fluids, and faster ramp capabilities. This work compares a waste heat recovery system based on an integrally geared compander in a sCO2 preheat cycle configuration with split recuperator with a recuperated ORC in the literature. The integrally geared system is comprised of an 1800 rpm generator with high-pressure and low-pressure pinions splitting a two-stage compressor and expander. Cycle constraints and design drivers, and optimization of the sCO2 system are described, along with current technology readiness and full-pressure full-temperature opera ting experience of the various components including compressors, expanders, heat exchangers, and other system components. Both cycles are paired with a commercial 15 MW gas turbine, and the resulting system costs, performance, and other attributes are presented. The cycles are compared with an cold-side temperature of 35 °C, showing an ORC system output of 5066 kW and an sCO2 system output of 5660 kW, i.e. an 11.7 % performance benefit for sCO2. Additionally, cost and size requirements and costs for the sCO2 and ORC-based systems are compared, indicating comparable nominal costs for both systems and a potentially lower cost for sCO2 systems, particularly when an indirect heat transfer loop is needed.
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