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Effects of Tower Motion on Packing Efficiency

机译:塔式运动对包装效率的影响

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This work reviews the major published studies, both theoretical and experimental, that address the impact of wave motion onpacked tower performance. Current practice is to add excess packing to guarantee the required separation is obtained, thoughthere is little data available to derive a safety factor for packing height. This work highlights deficiencies in the currentknowledge base and analyzes general trends to address common misconceptions about tower design for floating production. Tilt and motions imposed on a fractionation column have a significant impact on product specifications due to reducedpacking efficiency. Improved awareness of motion impacts will assist the analysis of tower design and allow feedback to theprocess design. Identifying gaps in available data shows limits in the current understanding and allows the development ofappropriate simplifying assumptions. The current understanding of towers in motion allows only very basic design rules and the safety factor for packing heightin literature varies from 1.1 to 2.0. This provides little confidence in the ability to predict packing efficiency for floatingproduction. Static tilt is more detrimental to liquid distribution than motion at a given amplitude. Still, liquid maldistribution frommotion approaches that of static tilt as the period increases. Liquid sloshing, often cited as a significant concern, is arelatively minor contribution to maldistribution except for short periods and tall towers. The relative bed size has asignificant impact on liquid maldistribution, limiting the recommended maximum bed height:column diameter to 2 – 3 tomaximize the efficiency. Approach to equilibrium is often overlooked as the major determinant of sensitivity of efficiency to maldistribution.Separations that operate near equilibrium are more sensitive to maldistribution than services with a large driving force. Thus,distillation towers are generally more sensitive to motion than absorbers and sensitivity may vary over column height.Recommendations are provided for a bed-by-bed analysis and feedback to the process design. Floating production units require additional complexity and conservatism in tower design. An improved awareness ofmotion effects on towers, and the factors involved, will lead to improved designs and a reduction in the cost of floatingproduction facilities.
机译:这项工作审查了主要发表的研究,理论和实验,解决了波动托管塔性能的影响。目前的做法是添加多余的包装以保证获得所需的分离,尽管可以获得填充高度的安全系数很少有可用的数据。这项工作突出了当前知识基础的缺陷,并分析了普遍趋势,以解决浮动生产塔设计的常见误解。倾斜和在分馏栏上施加的动作由于减少的包装效率而对产品规格产生了重大影响。提高了运动影响的意识将有助于分析塔设计并允许反馈到工业设计。在可用数据中识别间隙显示当前了解的限制,并允许开发的简化假设。目前对运动中的塔的理解只有非常基本的设计规则,包装高度文献的安全系数从1.1到2.0变化。这提供了对预测浮动生产的包装效率的能力提供了很少的令人信心。静态倾斜对液体分布更有害,而不是给定幅度的运动。仍然,随着期间的增加,液体陈列措施从各种过程中接近静态倾斜度。除了短时间和高大的塔外,液体晃动通常被认为是一个重要的关注,对恶性来说是对恶性起步的贡献。相对床尺寸对液体陈列液的影响显着影响,限制了推荐的最大床高:柱直径至2 - 3截面的效率。均衡的方法通常被视为作为效率敏感性的主要决定因素,其对均衡的效率的敏感性。邻近均衡操作的分解比具有大驱动力的服务更敏感。因此,蒸馏塔通常对运动比吸收剂更敏感,并且灵敏度可以在柱高度上变化。提供用于床上床分析和对过程设计的反馈。浮动生产单位需要塔设计中的额外复杂性和保守主义。改善对塔楼的影响以及所涉及的因素,将导致改进的设计和降低浮动生产设施的成本。

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