凝结水稳定剂驱油诊断

Abdullah Al Sabri, Vipin Dua, Wasik Abeebur Rahman, Mufleh Idris, Muddassir Hameed, A. Kindi
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引用次数: 0

摘要

PDO Saih Rawl中央处理厂的凝析油稳定剂经历了严重的早熟水淹,导致工艺中断和操作困难。传统的稳态模拟和托盘水力学不能说明实际原因。本文的目的是介绍在分析洪水问题和确定的解决方案时所采用的方法。最初,通过与托盘供应商协商进行最新进料组成和托盘充分性检查的稳态过程模拟,分析了水淹问题。该研究得出结论,现有的硬件是足够的,射流驱油极限和下角驱油水平完全在可接受的范围内。该研究建议仅对操作条件进行少量调整以解决问题。作为核查的一部分,还联系了替代托盘供应商进行托盘液压检查,没有发现任何问题。随后,在正常操作过程中对储层进行伽马射线扫描,并在模拟柱内注水后重复扫描。结合伽玛射线扫描结果,进行了逐层模拟,确定了水淹现象。伽马射线扫描显示了正常运行和模拟扰动条件下的柱内部状况、液体高度和泡沫水平。尽管托盘处于良好状态,但底部几个托盘在正常操作过程中显示出较高的液体高度。随着伽马射线扫描的结果,过程模拟结果和操作条件的调查揭示了水淹问题的可能原因。该研究预测,在几个塔盘中温度会下降,并在塔顶附近进一步上升,这对精馏塔来说是不寻常的。这是原始设计中不同进料比的结果,其中一个进料到塔的温度估计低于5°C,与塔的轮廓相比太冷了。根据研究结果,开发了在不影响柱形剖面生产能力的情况下缓解水淹问题的方案。在处理不同进料和大的温度变化时,塔内所经历的驱油性质是凝析液稳定剂所特有的。传统的全塔稳态模拟和托盘尺寸计算不足以研究这一问题。在正常作业和模拟驱油工况下,需要进行伽马射线扫描。
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Condensate Stabilizer Flooding Diagnosis
Condensate stabilizers at PDO Saih Rawl Central Processing Plant experienced severe pre-mature flooding causing process upsets and Operational difficulties. Conventional steady state simulations and tray hydraulics could not suggest actual causes. The purpose of the proposed paper is to present the methods followed in analyzing the flooding issue and identified solutions. Initially, the flooding issue was analyzed by carrying out steady state process simulation with latest feed composition and tray adequacy checks in consultation with the tray supplier. The study concluded the existing hardware is adequate, jet flooding limit and down comer flooding levels well within acceptable limits. The study recommended only few adjustments in Operating conditions to resolve the issue. As part of verification, alternate tray suppliers were also approached to carry out tray hydraulic checks and found no concerns. Subsequently, the column was subjected to gamma ray scan during normal operation and a scanning was repeated after simulating a flooding inside the column. Coupled with gamma ray scanning results, a tray by tray by simulation was carried out to ascertain the flooding the phenomena. Gamma ray scan revealed the condition of the column internals, liquid heights and froth level during normal operation as well as during simulated upset conditions. Even though the trays were in good conditions, bottom few trays showed higher liquid height during normal operation itself. Along with the results from Gamma ray scanning, process simulation results and investigation of Operating conditions revealed the possible reasons for the flooding issue. The study predicted a temperature dip in few trays and further rise somewhere near the column top, which is unusual for a distillation column. This is the resultant of different feed ratios from the original design and one of the feed to the column is estimated to be below 5 °C, which is too cold compared to column profile. Based on the results, options were developed to alleviate the flooding issue without compromising the production capabilities of the column profile. The nature of flooding experienced inside the column handling different feeds and large variation in temperatures is unique with the condensate stabilizers. Conventional full column steady state simulation and tray sizing were not adequate for investigating problem. It needed, gamma ray scanning while the column is in normal operation and during simulated flooding condition.
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