甲烷水合物生产井电潜泵设计——以南开槽式甲烷水合物为例

IF 2.6 Q3 ENERGY & FUELS Upstream Oil and Gas Technology Pub Date : 2020-10-01 DOI:10.1016/j.upstre.2020.100023
Sukru Merey , Hakki Aydin , Tuna Eren
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引用次数: 6

摘要

天然气水合物行业的目标是在积累短期天然气水合物生产试验经验的基础上,进行长期天然气水合物生产试验。在天然气水合物生产试验中,大多采用电潜泵(ESP)对天然气水合物储层进行降压。然而,在天然气水合物井中ESP系统的使用和设计方面存在知识空白。因此,本研究旨在针对日本南开海槽甲烷水合物储层条件下的甲烷水合物生产井设计电潜泵系统。为此,我们编写了一套python代码来设计天然气水合物井中的ESP,并使用HEP模拟器来预测甲烷水合物通过ESP生产管柱采气过程中沿井筒形成天然气水合物的风险。研究表明,产水量(50-794 m3/天)的较大差异会对泵的性能产生负面影响,特别是在建议的泵工作流量之外。此外,由于生产过程中水流量的巨大差异,泵的效率在泵工作流量外从70 s%下降到20 s%。与常规气井不同的是,在天然气水合物井中,电机产生的温升对于避免任何气体水合物的形成至关重要,而温升受操作频率的影响。在40 Hz工作频率以上,随着频率的增加,电机使井温升高(近0.65 ~ 1.75℃),有利于防止井内形成天然气水合物。在泵的功率要求上,海面采出水和将采出水排放到海底没有区别。根据ESP生产过程中井筒内甲烷水合物平衡预测,在设计条件下不容易形成甲烷水合物。然而,当ESP发生故障时,由于井筒压力升高、井温降低,可能会在井内形成甲烷水合物。
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Design of electrical submersible pumps in methane hydrate production wells: A case study in Nankai trough methane hydrates

Gas hydrate industry aims to conduct long-term gas hydrate production trials after gaining the experiences in short-term gas hydrate production trials. Electrical submersible pumps (ESP) were mostly chosen in gas hydrate production trials to depressurize gas hydrate reservoirs. However, there is a knowledge gap about the usage and design of ESP systems in gas hydrate wells. Therefore, in this study, it is aimed to design ESP systems in methane hydrate production well in the conditions of Nankai Trough (Japan) methane hydrate reservoirs. For this purpose, a set of python codes was written to design ESP in the case study gas hydrate well and also HEP simulator was used to predict gas hydrate formation risks along the wellbore during gas production from methane hydrates via ESP production string. It was shown that high variances in water production rates (50–794 m3/day) affect the pump performance negatively, especially in the outside of suggested pump working flow rates. Moreover, pump efficiencies decrease from 70 s% to 20 s% in the outside of pump working flow rates due to huge variances in water flow rates during production. Different than conventional gas wells, the temperature rise generated by the motor is important to avoid any gas hydrate formation in gas hydrate well, which was affected by the operating frequency. Above 40 Hz of operating frequency, well temperature increases (nearly 0.65–1.75°C) by the motor with increasing frequency, which is good for the prohibition of gas hydrate formation in the well. In terms of pump power requirements, there is no difference of producing water at sea surface and releasing produced water to the seafloor. According to the methane hydrate equilibrium predictions in the wellbore during production with ESP, methane hydrate is not like to form in the design conditions. However, with ESP malfunction, methane hydrate might form inside the well due to increasing wellbore pressure and decreasing well temperature.

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