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Key issues and practical design for cooling wall of supercritical carbon dioxide coal-fired boiler

机译:超临界二氧化碳燃煤锅炉冷却壁的关键问题及实用设计

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摘要

When supercritical carbon dioxide (S-CO2) Brayton cycle is used for coal-fired power plants, the significantly increased mass flow rate and endothermic temperature of S-CO2 boiler leads to the over-temperature and high pressure drop on the cooling wall (CW). This paper presents a mathematic flow and heat transfer model of S-CO2 in combustion chamber CW. The results show that reducing the tube diameter can effectively reduce the temperature difference in cooling wall and reduce the effect of high heat flux on the temperature difference. The pressure drop decreases exponentially with the increase of tube diameter and boiler expansion factor. Increasing partial flow numbers will decrease the boiler pressure drop and improve system cycle efficiency in spite of increasing the temperature difference of CW. The change of flow direction has no obvious effect on temperature distribution of CW and has opposite effect on gravity and buoyancy force. Three boiler layout strategies, including partial flow strategy, flow symmetry strategy and boiler local expansion strategy are proposed in order to coordinate the pressure drop and uneven temperature distribution, which can not only decrease boiler heat exchange surface temperature difference but also reduce the boiler pressure drop to prevent the over-temperature and improve system performance. (C) 2019 Elsevier Ltd. All rights reserved.
机译:当超临界二氧化碳(S-CO2)布雷顿循环用于燃煤电厂时,S-CO2锅炉的质量流量和吸热温度显着提高,导致冷却壁(CW)过热和高压降)。本文提出了燃烧室连续波中S-CO2的数学流动和传热模型。结果表明,减小管径可以有效减小冷却壁的温差,减小高热通量对温差的影响。压力降随管径和锅炉膨胀系数的增加呈指数下降。尽管增加了连续水的温差,但增加部分流数将减少锅炉压降并提高系统循环效率。流动方向的变化对连续波的温度分布没有明显影响,而对重力和浮力却有相反的影响。为了协调压降和温度分布不均匀,提出了三种锅炉布局策略,包括局部流策略,流对称策略和锅炉局部扩展策略,它们不仅可以减小锅炉换热表面温差,而且可以减小锅炉压降。以防止过热并改善系统性能。 (C)2019 Elsevier Ltd.保留所有权利。

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