首页> 外文期刊>Thermal engineering >The Effect of Heat-and-Mass Transfer and Flow Hydrodynamics on the Flow Accelerated Corrosion Rate in Evaporators of Combined-Cycle Unit Heat-Recovery Steam Generators
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The Effect of Heat-and-Mass Transfer and Flow Hydrodynamics on the Flow Accelerated Corrosion Rate in Evaporators of Combined-Cycle Unit Heat-Recovery Steam Generators

机译:热传质动力学对组合循环单元热回收蒸汽发生器蒸发器流动加速腐蚀速率的影响

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摘要

Abstract Flow accelerated corrosion (FAC) is considered one of the major causes of damage to heat-recovery steam generators (HRSG) of combined-cycle units. In the last few decades, a great number of papers devoted to this problem have been published in many countries around the world. The results of investigations were analyzed as a rule, on the basis of the flow-averaged thermochemical parameters of the flow, while the features of the near-wall liquid film determining the FAC rate were not taken into account. The indicators in the near-wall region depends on the heat-and-mass transfer conditions, flow hydrodynamics, and the specific of chemicals used to correct the water chemistry (WC). For ammonia and oxygen water treatment chemistries, an equilibrium model is proposed and its validity for HRSG evaporators is substantiated. The rate of the exchange of gas reagents between steam and water is determined by the distribution coefficient Kd. To simplify calculations, simple approximating correlations of Kd for ammonia and oxygen is recommended. For the water chemistry with solid reagents, a diffusion model has been developed to calculate mass transfer on the basis of data on heat transfer in steam-generating tubes. The concentration of reagents near the wall is determined by both the turbulent transport of the liquid between the flow core and the near-wall layer and the coefficient of reagent distribution between the phases. Simple approximating correlations of distribution coefficients for Na3PO4, NaOH, and 90H Turb helamine are proposed. An approximate correlation between the hydraulic resistance coefficient Kh and the geometric parameter Kс of the FAC process has been established. The hydrodynamic fundamentals of the standard HRSG structural members have been studied in more detail than FAC. To estimate Kс, one can use the known value of Kh and the correlation between them. However, this correlation should be used with care since it has been obtained for certain conditions of unambiguity (i.e., specific construction material, water chemistry, flow history, etc.). Under other conditions, this correlation will change somewhat; therefore, it can only be used for rough estimation.
机译:摘要流动加速腐蚀(FAC)被认为是损坏循环单元的热回收蒸汽发生器(HRSG)损坏的主要原因之一。在过去的几十年中,致力于这个问题的大量论文已在世界各国出版。根据流量的流量平均热化学参数,分析了研究结果,而近壁液膜的特征没有考虑确定基于壁的液体膜的特征。近壁区域中的指示器取决于热量传质条件,流动流体动力学,以及用于校正水化学(WC)的化学物质的具体。对于氨和氧水处理化学品,提出了平衡模型,并且证实了HRSG蒸发器的效力。蒸汽和水之间的气体试剂交换的速率由分布系数Kd确定。为了简化计算,建议使用KD对氨和氧气的简单近似相关性。对于具有固体试剂的水化学,已经开发了一种扩散模型以基于蒸汽发生管中的传热数据来计算质量转移。壁附近的试剂浓度由流动芯和近壁层之间的液体的湍流传输和相位之间的试剂分布系数来确定。提出了Na3PO4,NaOH和90H和90H型螺旋晶的分布系数的简单近似相关性。已经建立了液压电阻系数Kh与FAC工艺的几何参数KС之间的近似相关性。标准HRSG结构构件的流体动力学基本原理已比FAC更详细地研究。为了估计KС,可以使用已知的KH值和它们之间的相关性。然而,这种相关性应与护理一起使用,因为它已经获得了某些不曼比的条件(即,特定的建筑材料,水化学,流动历史等)。在其他条件下,这种相关性会有所改变;因此,它只能用于粗略估计。

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