水下管道设计中的流动保障——以加纳Jubilee和TEN油田为例

S. A. Marfo, Prince Opoku Appau, J. Acquah, E. M. Amarfio
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摘要

加纳Cape Three Point海上区块的勘探和生产活动不断增加,除了产生大量凝析气的油田外,还发现和开发了凝析气田。这些发现需要管道输送流体,以避免水合物和蜡的形成。本文重点介绍了使用Pipesim软件进行海底管道设计,该软件解决了从Jubilee和TEN油田向Atuabo天然气处理厂输送凝析气的流动保证问题。该公司还考虑了另一种设计方案,该方案消除了为实现2030年最高预计流量而增加管线容量的需求。该设计包括两个立管和两个流管。在3000 psig压力下,水合物形成温度为72.5˚F。管线1和管线2的绝缘厚度确定为1.5英寸。2英寸。分别。管线1和管线2的管径为12英寸。14英寸。分别。最大设计流量为150 MMSCFD。为了在2030年达到700万立方英尺/天的最高预计流量,16英寸/天的管道将被投入到生产中。长度为44公里的内径管道与12英寸管道平行放置。ID流程1。该平行管道将设计流量提高了约4.7倍(705 MMSCFD)。另一种设计采用了18英寸。20英寸。分别为流程1和2的内径管道。关键词:凝析气;流线;流保证;水合物;Pipesim
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Flow Assurance in Subsea Pipeline Design - A Case Study of Ghana’s Jubilee and TEN Fields
The increasing exploration and production activities in the offshore Cape Three Point Blocks of Ghana have led to the discovery and development of gas condensate fields in addition to the oil fields which produce significant amount of condensate gas. These discoveries require pipelines to transport the fluids avoiding hydrates and wax formation. This paper focuses on subsea pipeline design using Pipesim software that addresses flow assurance problems associated with transporting condensate gas from the Jubilee and TEN Fields to the Atuabo Gas Processing Plant. It also considered an alternate design that eliminates the need for capacity increase of flowlines for the futuristic highest projected flow rates in 2030. The design comprises of two risers and two flowlines. Hydrate formation temperature was determined to be 72.5 ˚F at a pressure of 3 000 psig. The insulation thickness for flowlines 1 and 2 were determined to be 1.5 in. and 2 in. respectively. The pipe size for flowlines 1 and 2 were determined to be 12 in. and 14 in. respectively. The maximum designed flow rate was determined to be 150 MMSCFD. To meet the highest projected flow rate of 700 MMSCFD in the year 2030 at the processing plant, a 16 in. ID pipeline of 44 km length was placed parallel to the 12 in. ID flowline 1. This parallel pipeline increased the designed flow rate by approximately 4.7 times (705 MMSCFD). The alternate design employs 18 in. and 20 in. ID pipes for flowlines 1 and 2 respectively. Keywords: Condensate Gas; Flowline; Flow Assurance; Hydrate; Pipesim
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