Investigation of Gas-liquid Separation Experiment of Electric Pump Drainage and Gas Extraction Unit in High Gas-liquid Ratio Gas Wells

Abstract Given the prominent problem of water in the Tarim basin of China with high formation temperature and large water production, a preferred scheme of electric pump drainage and gas extraction unit for gas fields with a high gas-liquid ratio is proposed by the mechanical principle and structura...

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Published inJournal of physics. Conference series Vol. 2659; no. 1; pp. 12033 - 12041
Main Authors Zhang, Bao, Jing, Hongtao, Tu, Zhixiong, Cui, Hangbo, Bai, Xiaofei, Zhou, Huaiguang, Yu, Xiaotong, Fan, Dabin, Xue, Longlong, Liu, Taochou
Format Journal Article
LanguageEnglish
Published Bristol IOP Publishing 01.12.2023
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Summary:Abstract Given the prominent problem of water in the Tarim basin of China with high formation temperature and large water production, a preferred scheme of electric pump drainage and gas extraction unit for gas fields with a high gas-liquid ratio is proposed by the mechanical principle and structural design method. Then, the corresponding electric pumps were developed, and the drainage and gas extraction scheme of a permanent magnet electric pump unit with gas-liquid separation in the way of an inverted deflector is designed. Through indoor experiments simulating the downhole gas-liquid ratio environment, the gas-liquid separation ability and adaptability of the design scheme under different good conditions are verified. The results obtained demonstrate that the cable connection process can meet the requirements of high-pressure resistance (≥25 MPa), and the gas-liquid separation effect is very good in vertical wells by adopting the inverted deflector scheme. The separation effect exceeded 90% under different working conditions (production from 30 to 150 m 3 /day and inhalation gas-liquid ratio from 50% to 95% and even higher) in the experiment with high gas content. The results will promote the gas recovery rate of high gas-liquid ratio gas fields and improve extraction efficiency.
ISSN:1742-6588
1742-6596
DOI:10.1088/1742-6596/2659/1/012033