节能气体脱水的改进再生方案

Haseeb Ali, S. Sajjad
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引用次数: 0

摘要

分子筛脱水装置用于天然气加工或运输前的脱水。分子筛脱水系统由多个吸附器组成,这些吸附器在吸附循环中除去水分,直到它们被水饱和。饱和吸附器的再生是通过使热再生气流通过吸附器来进行的。热再生气体通过吸附器后,冷却后送至再生气体压缩。如果使用风冷交换器来冷却热再生气体,则热再生气体中可用的热量最终会进入大气。在这种情况下,进行了一项内部研究,以检查在一个气体处理地点使用改进的再生方案从热废再生气体中回收废热的技术经济可行性。修改后的方案包括安装一个新的废热回收(WHR)交换器,将热再生气体中的可用热量与再生加热器的入口再生气体交换,从而减少再生加热器的燃料气体消耗以及再生气体冷却器风扇的功耗。该研究包括设计和操作数据的收集和分析,然后对关键挑战进行评估。关键的挑战包括加热器在高冷工况下的性能(即更低的燃料气体消耗),新高冷换热器的空间可用性以及对现有系统的修改。开发了一个热力学模型,用于运行各种操作场景并估计WHR潜力,包括加热器在不同温度下的特定燃气消耗分析,以建立实际的燃气节约。总体而言,这项研究表明,拟议的再生方案节省了大量能源,财务指标良好。它还显示减少了加热器和冷却器的峰值热负荷,从而为未来的项目提供了减少资本支出的额外优势。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Modified Regeneration Scheme for Energy Efficient Gas Dehydration
Molecular Sieve Dehydration units are used for dehydration of natural gas prior to gas processing or transportation. A molecular sieve dehydration system consists of multiple adsorbers which remove water during adsorption cycle until they get saturated with water. Regeneration of a saturated adsorber is performed by passing a hot regeneration gas stream through the adsorber. The hot regeneration gas after passing though the adsorber is then cooled before sending to regeneration gas compression. If an aircooled exchanger is used to cool the hot regeneration gas, heat available in the hot spent regeneration gas ends up in the atmosphere. In this context, an in-house study was performed to examine techno-economic viability of waste heat recovery from the hot spent regeneration gas using a modified regeneration scheme at one of the gas processing sites. The modified scheme involves installation of a new waste heat recovery (WHR) exchanger to exchange the heat available in the hot regeneration gas with regeneration heater's inlet regeneration gas thereby reducing the fuel gas consumption in the regeneration heater as well as power consumption in regeneration gas cooler fans. The study comprised design and operation data collection and analysis followed by assessment of key challenges. The key challenges include performance of the heater in WHR case (i.e. lower fuel gas consumption), space availability for the new WHR exchanger and modifications in the existing system. A thermodynamic model was developed for running various operating scenarios and estimating the WHR potential, including heater's specific fuel gas consumption analysis at varying temperatures, to establish realistic fuel gas savings. Overall, the study has indicated significant energy savings with good financial indicators for the proposed regeneration scheme. It has also showed reduction of peak heat duty of heater & cooler, thus providing an additional advantage of reduced CAPEX for future projects.
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