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Experimental and numerical study of a micro-cogeneration Stirling unit under diverse conditions of the working fluid

机译:微工热斯特林装置在不同工质条件下的实验和数值研究

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摘要

Micro-cogeneration Stirling units are promising for residential applications because of high total efficiencies, favorable ratios of thermal to electrical powers and low CO as well as NOx emissions. This work focuses on the experimental and the numerical analysis of a commercial unit generating 8 kW of hot water (up to 15 kW with an auxiliary burner) and 1 kW of electricity burning natural gas. In the experimental campaign, the initial pressure of the working fluid is changed in a range from 9 to 24 barg – 20 barg being the nominal value – while the inlet temperature of the water loop and its mass flow rate are kept at the nominal conditions of, respectively, 50°C and 0.194 kg/s. The experimental results indicate clearly that the initial pressure of the working fluid – Nitrogen – affects strongly the net electrical power output and efficiency. The best performance for the output and efficiency of 943 W and 9.6% (based on the higher heating value of the burnt natural gas) are achieved at 22 barg. On the other hand, the thermal power trend indicates a maximum value of 8420 W at the working pressure of 24 barg, which corresponds to a thermal efficiency of 84.7% (again based on higher heating value). Measurements are coupled to a detailed model based on a modification of the work by Urieli and Berchowitz. Thanks to the tuning with the experimental results, the numerical model allows investigating the profiles of the main thermodynamic parameters and heat losses during the cycle, as well as estimating those physical properties that are not directly measurable. The major losses turn to be the wall parasitic heat conduction from heater to cooler and the non-unitary effectiveness of the regenerator.
机译:微型热电联产斯特林装置具有很高的总效率,有利的火电比,低的CO和NOx排放,因此有望用于住宅应用。这项工作的重点是对商用单位产生8 kW热水(使用辅助燃烧器可达15 kW)和1 kW燃烧天然气的商业单位进行实验和数值分析。在实验过程中,工作流体的初始压力在9至24 barg(标称值为20 barg)的范围内变化,而水环路的入口温度及其质量流量保持在标称条件下。分别为50°C和0.194 kg / s。实验结果清楚地表明,工作流体的初始压力-氮气-会严重影响净电功率输出和效率。在22 barg的压力下,输出和效率的最佳性能分别为943 W和9.6%(基于燃烧天然气的较高热值)。另一方面,热功率趋势指示在24 barg的工作压力下的最大值为8420 W,这对应于84.7%的热效率(同样基于较高的发热量)。根据Urieli和Berchowitz对工作的修改,将测量与详细模型耦合。通过对实验结果的调整,数值模型可以研究循环过程中主要热力学参数和热量损失的分布,并估算出无法直接测量的物理性质。主要的损失变成了从加热器到冷却器的壁面寄生热传导以及蓄热器的非整体效率。

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