Thermal optimization of embedded thermoelectric generators in refractory furnaces

K. Yazawa, A. Shakouri
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引用次数: 3

Abstract

Industrial energy consumption represents a large part of the energy flow in the United States and it would probably be similar in many other countries. Coal or gas fired furnaces are a major component of the energy consumption to supply high temperatures. Refractory wall is indispensable along the furnace pathway designed for melting or processing materials. Unfortunately, more than a fraction of the input energy diffuses across the refractory wall due to the high temperatures and the waste heat is dumped to the ambient. Thermoelectric power generator (TEG) has an ultra low profile and is widely scalable with arraying the modules. This configuration is matched very well with the requirement of harvesting energy from the waste heat through the refractory wall without any design change of the current furnaces. We propose a simple water-cooled TEG system replacing a fraction of the refractory wall thickness while maintaining the melt temperature and the heat flux would be the same as the current refractory wall with passive air cooling. Design optimization is conducted, trading-off the TEG module thickness and the furnace wall thickness maximizing the power output while maintaining the above heat flux. We will present a quantitative analysis based on an example of the conventional fire ports that produce furnace gases at a temperature of 1500 °C. The furnace is designed for melting glass pellets and maintaining the temperature of melt glass at 1000 °C in a pool. A facility with 500 ton/day capacity is modeled. There are four fire ports and 54 cm thick aluminum-zirconia-silica (AZS) refractory wall around the ports. The thermal optimization is conducted considering the design of TEG matched to desired heat flux of approximately 10 kW/m2. As shown in our earlier work, the TEG design with a smaller TE element fill factor down to 10% or below, will provide the most cost effective power generation. Interestingly, the additional material cost for the optimum TEG with 10% fill factor and a copper cold plate is much less expensive compared to the cost needed for the AZS refractory wall material that it is replacing. When the remaining thickness of the refractory wall is 25 cm, the power generation from TEG is 1.72 kW/m2 while maintaining the same heat flux. The total power output from the all four fire ports can be 66.1 kW and the cost for the TEG module is estimated to be $0.5 per Watt based on demonstrated robust high temperature TE material.
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难熔炉嵌入式热电发电机的热优化
工业能源消耗占美国能源流动的很大一部分,在许多其他国家可能也是如此。燃煤或燃气炉是提供高温能源消耗的主要组成部分。耐火壁是为熔化或加工材料而设计的炉道上不可缺少的部分。不幸的是,由于高温,超过一部分的输入能量扩散穿过耐火墙,余热被倾倒到环境中。热电发电机(TEG)具有超低的外形和广泛的可扩展的模块阵列。这种结构非常符合在不改变现有炉体设计的情况下,通过耐火壁从废热中收集能量的要求。我们提出了一种简单的水冷TEG系统,在保持熔体温度和热流密度与目前采用被动空气冷却的耐火壁相同的情况下,替换部分耐火壁厚度。进行设计优化,在保持上述热流密度的同时,权衡TEG模块厚度和炉壁厚度,使输出功率最大化。我们将根据一个在1500°C温度下产生炉气的传统火口的例子进行定量分析。该炉设计用于熔化玻璃球团,并在池中保持熔融玻璃的温度在1000°C。以500吨/天的生产能力为模型。有4个火口,火口周围有54 cm厚的AZS耐火墙。考虑热流密度约为10 kW/m2的TEG设计,进行了热优化。正如我们之前的工作所示,TEG设计具有较小的TE元件填充系数,可降至10%或以下,将提供最具成本效益的发电。有趣的是,具有10%填充系数的最佳TEG和铜冷板的额外材料成本,与它所取代的AZS耐火壁材料所需的成本相比要便宜得多。当耐火壁剩余厚度为25cm时,在保持相同热流密度的情况下,TEG发电量为1.72 kW/m2。所有四个消防端口的总输出功率可达66.1 kW,基于已演示的坚固的高温TE材料,TEG模块的成本估计为每瓦0.5美元。
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