How Dry Is Dry?

C. Hartloper, K. Botros, V. Liu, G. Lalonde, J. Lu, Y. Saud de Puche
{"title":"How Dry Is Dry?","authors":"C. Hartloper, K. Botros, V. Liu, G. Lalonde, J. Lu, Y. Saud de Puche","doi":"10.1115/IPC2018-78580","DOIUrl":null,"url":null,"abstract":"Air drying is used after dewatering to dry a pipeline or piping facility before commissioning it with natural gas. This process typically involves blowing dehydrated air through the pipe sections until they are determined to be suitably dry. The question addressed in this paper is: how dry is dry? A common metric used to judge the pipe section’s dryness is the drying air’s outlet water dew point. Typically, air drying continues until a suitably dry low water dew point, such as −40°C, is measured at the outlet of the pipeline or facility. However, there is currently a lack of understanding of how this final outlet water dew point relates to the remaining water and thus the subsequent start up of the pipeline or facility. If the outlet water dew point is higher than required, issues may arise upon start up; e.g., hydrates could form along the pipeline or at downstream facilities. Conversely, if the outlet water dew point is lower than required, unnecessary time would have been spent in drying, and hence higher cost.\n This paper advocates an approach to determine when air drying is complete that considers the start-up phase. The approach consists of two parts. In the first part, the air drying parameters (drying air flow rate, inlet water dew point, etc.) and the final outlet water dew point are used to quantify the volume and surface area of water remaining after the drying process is completed. In the second part, the evaporation of this water into the gas flowing through the pipeline/facility after commissioning and start up is modeled as a function of the gas flow rate, temperature, pressure and inlet water content. Then, the water content of the gas at the delivery points is calculated. This increase can then be evaluated in reference to the water content specifications at the delivery points. The approach is exemplified by a 31 km NPS 48 pipeline over a mountainous terrain.","PeriodicalId":164582,"journal":{"name":"Volume 2: Pipeline Safety Management Systems; Project Management, Design, Construction, and Environmental Issues; Strain Based Design; Risk and Reliability; Northern Offshore and Production Pipelines","volume":"450 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"2018-09-24","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Volume 2: Pipeline Safety Management Systems; Project Management, Design, Construction, and Environmental Issues; Strain Based Design; Risk and Reliability; Northern Offshore and Production Pipelines","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1115/IPC2018-78580","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0

Abstract

Air drying is used after dewatering to dry a pipeline or piping facility before commissioning it with natural gas. This process typically involves blowing dehydrated air through the pipe sections until they are determined to be suitably dry. The question addressed in this paper is: how dry is dry? A common metric used to judge the pipe section’s dryness is the drying air’s outlet water dew point. Typically, air drying continues until a suitably dry low water dew point, such as −40°C, is measured at the outlet of the pipeline or facility. However, there is currently a lack of understanding of how this final outlet water dew point relates to the remaining water and thus the subsequent start up of the pipeline or facility. If the outlet water dew point is higher than required, issues may arise upon start up; e.g., hydrates could form along the pipeline or at downstream facilities. Conversely, if the outlet water dew point is lower than required, unnecessary time would have been spent in drying, and hence higher cost. This paper advocates an approach to determine when air drying is complete that considers the start-up phase. The approach consists of two parts. In the first part, the air drying parameters (drying air flow rate, inlet water dew point, etc.) and the final outlet water dew point are used to quantify the volume and surface area of water remaining after the drying process is completed. In the second part, the evaporation of this water into the gas flowing through the pipeline/facility after commissioning and start up is modeled as a function of the gas flow rate, temperature, pressure and inlet water content. Then, the water content of the gas at the delivery points is calculated. This increase can then be evaluated in reference to the water content specifications at the delivery points. The approach is exemplified by a 31 km NPS 48 pipeline over a mountainous terrain.
干有多干?
空气干燥是在管道或管道设施脱水后进行干燥,然后再用天然气进行调试。这个过程通常包括吹脱水空气通过管道部分,直到确定它们是适当的干燥。本文要解决的问题是:到底有多干?判断管段干燥程度的常用指标是干燥空气的出水露点。通常情况下,空气干燥会继续进行,直到在管道或设施的出口测量到适当干燥的低露点,例如- 40°C。然而,目前缺乏对最终出水露点与剩余水之间的关系以及随后管道或设施的启动的理解。如果出水露点高于要求,启动时可能出现问题;例如,水合物可能沿着管道或在下游设施形成。相反,如果出水露点低于要求,则会花费不必要的时间进行干燥,从而增加成本。本文提倡一种考虑启动阶段的确定风干完成时间的方法。该方法由两部分组成。在第一部分中,利用空气干燥参数(干燥空气流速、入口水露点等)和最终出口水露点来量化干燥过程完成后剩余水的体积和表面积。在第二部分中,在调试和启动后,将这些水蒸发成流经管道/设施的气体,并将其建模为气体流速、温度、压力和进口含水量的函数。然后,计算输送点处气体的含水量。然后可以参照交付点的含水量规格来评估这种增加。该方法的例子是一条31公里长的NPS 48管道,该管道位于山区。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
求助全文
约1分钟内获得全文 求助全文
来源期刊
自引率
0.00%
发文量
0
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
确定
请完成安全验证×
copy
已复制链接
快去分享给好友吧!
我知道了
右上角分享
点击右上角分享
0
联系我们:info@booksci.cn Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。 Copyright © 2023 布克学术 All rights reserved.
京ICP备2023020795号-1
ghs 京公网安备 11010802042870号
Book学术文献互助
Book学术文献互助群
群 号:604180095
Book学术官方微信