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Inhibition of methane hydrate re-formation in offshore pipelines with a kinetic hydrate inhibitor

机译:用动力水合物抑制剂抑制海上管道中甲烷水合物的重整

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摘要

Methane gas from marine hydrate deposits can be produced by one or a combination of three methods; de-pressurization, thermal stimulation, and the injection of hydrate inhibitors. Because residual hydrate structures known as hydrate precursors will exist in the liquid water phase after dissociation, the risk of methane hydrate re-formation has to be evaluated during the production and transportation of methane gas through offshore pipelines. New experimental procedures composed of three stages are designed to simulate the dissociation of marine hydrates and the transportation of produced fluids. The obtained experimental results have shown that methane hydrates are rapidly re-formed when the temperature of dissociated water falls into the hydrate formation region during the cooling down process. The subcooling for three different dissociation pressures of 80, 70, and 60 bar were 1.3,1.2 and 1.6 °C, respectively. One viable option to avoid hydrate re-formation is injecting hydrate inhibitors before transporting the fluids through pipelines. Among various hydrate inhibitors, Poly(N-vinylcaprolactam) (PVCap) was selected as a possible candidate for a Kinetic Hydrate Inhibitor (KH1) and injected into dissociated water before cooling down the fluids. The concentration of PVCap was varied from 0.5 to 3.0 wt.%. With an increase in the PVCap concentration, the subcooling increased to 7.8 °C at a dissociation pressure of 80 bar, which suggests that the risk of hydrate re-formation can be reduced by injecting PVCap. Moreover it is observed that the subcooling increased to 8.8 °C at the PVCap concentration of 3.0 wt% in the presence of NaCl in the water phase. Although the use of KHI in conventional gas production has become common, its applicability to methane hydrate production has not yet been studied thoroughly, especially in the presence of residual hydrate structures. In this work, the application of KHI to methane hydrate production is discussed.
机译:来自海洋水合物沉积物的甲烷气体可以通过一种方法或三种方法的组合产生。减压,热刺激和注入水合物抑制剂。由于离解后的液态水相中将存在称为水合物前体的残留水合物结构,因此在通过海上管道生产和运输甲烷气体期间,必须评估甲烷水合物重整的风险。设计了由三个阶段组成的新实验程序,以模拟海洋水合物的离解和产出液的运输。获得的实验结果表明,在冷却过程中,当离解水的温度落入水合物形成区域时,甲烷水合物会迅速重整。三种不同的解离压力80、70和60 bar的过冷度分别为1.3、1.2和1.6°C。一种避免水合物重新形成的可行选择是在通过管道输送流体之前注入水合物抑制剂。在各种水合物抑制剂中,选择聚(N-乙烯基己内酰胺)(PVCap)作为动力学水合物抑制剂(KH1)的可能候选物,并在冷却流体之前将其注入离解水中。 PVCap的浓度为0.5至3.0重量%。随着PVCap浓度的增加,在80 bar的解离压力下,过冷度增加到7.8°C,这表明可以通过注入PVCap来降低水合物重整的风险。此外,观察到在水相中存在NaCl的情况下,在3.0wt%的PVCap浓度下,过冷度增加到8.8℃。尽管在常规的天然气生产中使用KHI已变得很普遍,但是其在甲烷水合物生产中的适用性尚未得到充分研究,特别是在存在残留水合物结构的情况下。在这项工作中,讨论了KHI在甲烷水合物生产中的应用。

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