首页> 外文会议>ASME international conference on ocean, offshore and arctic engineering >WAX DEPOSITION PREDICTION AND CONTROL IN WAXY CRUDE OIL TIEBACK FLOWLINES FOR SOUTH CHINA SEA DEEPWATER OIL DEVELOPMENT
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WAX DEPOSITION PREDICTION AND CONTROL IN WAXY CRUDE OIL TIEBACK FLOWLINES FOR SOUTH CHINA SEA DEEPWATER OIL DEVELOPMENT

机译:南海深水油田蜡质回潮油流中蜡沉积的预测与控制

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Crude oils are generally very complex chemical systems consisting predominantly of hundreds to thousands of hydrocarbon compounds from simple low-molecular-weight paraffin to high-molecular-weight waxes. There are many factors effecting wax deposition such as the fluid composition, pressure and temperature and so on. Wax deposition is complex dynamic process related to transient heat and mass transfer, therefore it is very difficult to predict wax deposition velocity accumulation amounts on the wall in waxy crude oil tieback flowlines. There exist many waxy crude oil tieback flowlines for South China Sea deepwater oil development, which can cause many flow assurance problems. It is very important to carry out wax deposition prediction calculation and effective measures are adopted to solve flow assurance problems. In this study, based on certain waxy crude oil tieback flowlines for South China Sea deepwater oil development, OLGA software is used to simulate transient flow characteristics in waxy crude oil tieback flowlines such as wax precipitation rate, thickness of wax layer deposited at wall, pigging frequency and so on. OLGA software simulation results is coincident with field pigging operation results, finally obtaining a good simulation methods to predict transient flow characteristics in waxy crude oil tieback flowlines and giving good suggestions to determine pigging periods and frequency. The study results show two 10 inch non-insulation steel flowlines are recommended to develop deepwater waxy crude oil field and pigging periods should comprehensive consider thickness of wax layer deposited at wall and the increase of pressure caused by wax deposition. It is reasonable to 35 days pigging periods during 2 year after put into production, 60 days pigging periods after 2 years. The results show maximum liquid flow rate for a 10 inch flowline is 7000m~3/d, and it is reasonable that one flowline is used to transport when flow rate is lower than 7000m~3/d, and two flowlines are used to transport when flow rate is more than 7000m~3/d. The pump pressure at FPSO is kept at 6000kPaA, and required maximum liquid flow rate of pigging at FPSO is 4200m7d(175m~3/h).
机译:原油通常是非常复杂的化学系统,主要由数百到数千种烃化合物组成,从简单的低分子量石蜡到高分子量蜡。有许多影响蜡沉积的因素,例如流体组成,压力和温度等。蜡沉积是与瞬态传热和传质相关的复杂动态过程,因此很难预测蜡质原油回输管线中壁上蜡沉积速度的累积量。南海深水石油开发存在蜡质原油回输流水线,会引起很多流动保障问题。进行蜡沉积预测计算非常重要,并采取有效措施解决流动保证问题。在这项研究中,基于用于南海深水石油开发的某些蜡质原油回注流线,使用OLGA软件模拟蜡质原油回注流线的瞬态流动特性,例如蜡的沉淀速率,沉积在壁上的蜡层厚度,清管。频率等。 OLGA软件的​​仿真结果与现场清管操作结果相吻合,最终获得了一种很好的模拟方法来预测蜡质原油回输管线中的瞬态流动特性,并为确定清管周期和频率提供了很好的建议。研究结果表明,建议使用两条10英寸非绝缘钢流水线开发深水蜡质原油油田,清管期应综合考虑沉积在壁上的蜡层厚度和由蜡沉积引起的压力增加。投产后2年内清管期为35天,2年后清管期为60天是合理的。结果表明,一条10英寸流水线的最大液体流速为7000m〜3 / d,当流速低于7000m〜3 / d时,一条流水线用于输送,当水流低于7000m〜3 / d时,两条流水线用于输送是合理的。流量大于7000m〜3 / d。 FPSO的泵压保持在6000kPaA,FPSO所需的最大清管液体流速为4200m7d(175m〜3 / h)。

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