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Numerical Feasibility Study of a Wax Cold Flow Approach for Subsea Tie-In Flowlines Using a 1D Mechanistic Multiphase Flow Simulator

机译:一维机制多相流模拟器对海底绑扎流水线蜡冷流方法的数值可行性研究

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This work is a thermo-fluid numerical case study to investigate the size and performance of a system that eliminates needs for insulating, heating and inhibiting chemically the deposition of wax in subsea tie-in flowlines. For short, we call this type of systems “Cold Flow”. The particular system analyzed in this study consists of a reactor unit at the inlet to the flowline, where the thermal solubility of the wax-creating molecules is reduced by cooling. Subsequently, solid wax is deposited in the reactor piping and wax free crude is entering the flowline. The reactor is regenerated periodically. The reactor-pipeline system was modelled using a commercial flowline simulator, with transient, thermal, multiphase and deposition capabilities. The basic layout used was a transportation pipeline of 8 km and 6.69 in ID with a mass flow rate of 17.51 kg/s, a water cut (WC) of zero and an inlet temperature of 70 style="white-space:nowrap;">°C. The wax appearance temperature (cloud point) of the crude is 22 style="white-space:nowrap;">°C and the seabed temperature is 4 style="font-family:Verdana;"> style="white-space:nowrap;">°C. Three types of reactors have been simulated: a non-insulated pipe section, a passive cooler with a bundle of parallel pipes and an active cooler. Sensitivity analyses have been performed for all three cases varying the external convective coefficient, the reactor pipeline diameter and the WC. For a non-insulated pipeline section cooler, the required length is of the same order of magnitude as the main flowline, implying that such a solution is impractical for short flowline distances or when a compact deployment is desired. For the passive cooler case, the required length was half of that in the previous case style="font-family:Verdana;">; style="font-family:Verdana;"> thus it is still significant. For the active cooler reactor, the required cooling duty was 2.2 MW. In all three cases, the pipe-flow dynamics were analyzed, and the pigging arrangement complexity has been qualitatively addressed. However, the detailed design falls out of the scope of this study.
机译:这项工作是一个热流体数值案例研究,旨在研究系统的尺寸和性能,该系统消除了对保温,加热和化学抑制蜡在海底连接流水线中沉积的需求。简而言之,我们称这类系统为“冷流”。在这项研究中分析的特定系统由在流水线入口处的反应器单元组成,在其中通过冷却降低产生蜡分子的热溶解度。随后,固体蜡沉积在反应器管道中,不含蜡的原油进入流水线。反应器定期再生。使用具有过渡,热,多相和沉积功能的商用流线模拟器对反应堆管道系统进行建模。所使用的基本布局是一条8公里长的管道,内径为6.69,质量流量为17.51 kg / s,含水率(WC)为零,入口温度为70 style =“ white-space:nowrap ;“>° C。原油的蜡相温度(浊点)为22 style =“ white-space:nowrap;”>° C,海底温度为4 style =“ font-family:Verdana;” > style =“ white-space:nowrap;”>° C。模拟了三种类型的反应堆:非绝缘管段,带有一捆平行管的被动式冷却器和主动式冷却器。对于所有三种情况都进行了敏感性分析,以改变外部对流系数,反应堆管道直径和WC。对于非绝缘的管道截面冷却器,所需的长度与主流线相同,这意味着对于较短的流线距离或需要紧凑的部署,这种解决方案是不切实际的。对于被动式散热器,所需长度是前一种情况的一半 style =“ font-family:Verdana;”>; style =“ font-family:Verdana; “>因此仍然很重要。对于主动冷却器反应堆,所需的冷却负荷为2.2 MW。在所有这三种情况下,均分析了管道流动动力学,并且定性地解决了清管布置的复杂性。但是,详细设计超出了本研究的范围。

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