中压过热器失活管性能退化分析

IF 16.4 1区 化学 Q1 CHEMISTRY, MULTIDISCIPLINARY
Ahmad Syafiq Haqim, W. W. Wan Mohamed, Al Hassan Salami Tijjani
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引用次数: 0

摘要

蒸汽在石油化工工业中作为热能的输送和一些重整过程的使用是必不可少的。过热器是一种热交换器,它利用烟气流中的余热将饱和蒸汽转化为干蒸汽。中压蒸汽过热器由于在高温下使用和蒸汽中存在液相的侵蚀,容易使管道变质,导致管道故障后堵塞。这减少了过热器的整体表面加热面积。管内堵塞与过热器能量动力学之间的关系对于工程师识别过热器的响应以进行运行规划具有重要意义,而这一问题在学术界尚未得到广泛的探讨。根据某石化蒸汽发生线的运行数据,分析了表面受热面积减小对过热器性能的影响。目的是找出管道堵塞对蒸汽和烟道气流状态的影响之间的关系,以及它对总能量交换的影响。通过第一定律能量分析,比较了某过热器在2014年堵管前和2017年堵管后两个独立服役年份的运行情况。平均蒸汽入口温度在248°C至250°C之间,流量在70至90吨/小时之间。分析表明,每堵一个管,需要增加0.3 ~ 0.8%的进口能量来补偿受热面的减小。当加热表面积减少3%时,热交换器的效率平均降低11%,这也导致蒸汽温度输出比设计工作温度降低约6%。这些结果将有助于蒸汽工程师分析整个工厂能源经济的变化,并决定用新过热器取代现有过热器的可行性。此外,蒸汽工程师需要考虑的另一个重要发现是,目前增加蒸汽流量的做法并不能抵消由于管道堵塞而造成的能量效率损失。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Performance degradation analysis of a medium pressure superheater due to tube deactivation
Steam is essential in petrochemical industries for the transportation of thermal energy and usage in some reforming process. Superheaters are heat exchangers that convert saturated steam to dry steam by utilizing waste heat from the flue gas stream. Medium pressure steam superheaters are prone to tube deterioration due to service at elevated temperatures and erosion from the presence of liquid phase in the steam, leading to tube plugging after tube failure. This reduces the overall surface heating area of the superheater. Relations between the tube plugging practice and the energy dynamics of the superheaters are important for engineers to identify the responses of the superheater for operation planning, and this issue has not been extensively explored academically. This article analyses the deterioration of superheater performance due to reduction of surface heating area based on operational data of a petrochemical steam generation line. The objective is to find relations between the effect of tube plugging on the states of both steam and flue gas streams, as well as its impact on the overall energy exchange. The operating conditions of a superheater at two separate service years, before (year 2014) and after (year 2017) tube plugging, were compared through the first law energy analysis. The average steam inlet temperatures were between 248 °C and 250 °C, at flow rates between 70 and 90 ton/hour. The analysis indicated that 0.3 to 0.8 % increase in inlet energy is required for every plugged tube to compensate for the reduction of heating surface. At 3 % reduction of heating surface area, the heat exchanger effectiveness decreases by an average of 11 % that also leads to a lower steam temperature output by approximately 6% from the design operating temperature. These results would assist steam engineers to analyse changes to the energy economics of the whole plant and decide the feasibility of replacing existing superheaters with new ones. Also, another significant finding to be considered by steam engineers is that the current practice of increasing the steam flow rate does not offset the loss of energy effectiveness due to tube plugging.
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来源期刊
Accounts of Chemical Research
Accounts of Chemical Research 化学-化学综合
CiteScore
31.40
自引率
1.10%
发文量
312
审稿时长
2 months
期刊介绍: Accounts of Chemical Research presents short, concise and critical articles offering easy-to-read overviews of basic research and applications in all areas of chemistry and biochemistry. These short reviews focus on research from the author’s own laboratory and are designed to teach the reader about a research project. In addition, Accounts of Chemical Research publishes commentaries that give an informed opinion on a current research problem. Special Issues online are devoted to a single topic of unusual activity and significance. Accounts of Chemical Research replaces the traditional article abstract with an article "Conspectus." These entries synopsize the research affording the reader a closer look at the content and significance of an article. Through this provision of a more detailed description of the article contents, the Conspectus enhances the article's discoverability by search engines and the exposure for the research.
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