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Effect of compound sloshing conditions on pressure drop and heat transfer characteristics for FLNG spiral wound heat exchanger

机译:复合晃动条件对絮凝螺旋缠绕热交换器压降和传热特性的影响

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摘要

Floating liquefied natural gas (FLNG) is a promising floating production equipment which integrates the gas extraction, liquefaction, storage, loading and unloading of offshore liquefied natural gas. The spiral wound heat exchanger (SWHE) is one of the most important installations of FLNG and the effect of compound sloshing on the performance of the spiral wound heat exchanger attracts a lot of attention. In this work, an experimental device of dual mixed refrigerant (DMR) and a multi-phase four-stream calculation code for SWHE are constructed to study the performance of FLNG SWHE. Quantitative analysis of temperature, pressure drop and enthalpy affected by sloshing periods, displacements and types are completed. Compared with temperatures, pressure drop characteristics of SWHE are much more significantly influenced under sloshing conditions, especially for compound heaving and pitching conditions. The maximum fluctuation range of gas-phase mixed refrigerant pressure drop is from - 11.08% to 24.96% for steady state. The temperature of gas-phase mixed refrigerant increases by 6.45 degrees C and the heat exchange decreases by 37.90 W under compound heaving and pitching conditions.
机译:浮动液化天然气(FLNG)是一个有前途的浮动生产设备,其集成了海上液化天然气的气体提取,液化,储存,装卸。螺旋缠绕热交换器(SWHE)是FLNG最重要的装置之一,复合晃动对螺旋缠绕热交换器的性能的影响吸引了很多关注。在这项工作中,建立了一种双混合制冷剂(DMR)的实验装置和SWHE的多相四流计算代码,以研究FLNG SWHE的性能。完成了受晃动周期,位移和类型影响的温度,压降和焓的定量分析。与温度相比,SWHE的压降特性在晃动条件下的影响要显着影响,特别是对于复合的悬挂和俯仰条件。气相混合制冷剂压降的最大波动范围为稳态为-11.08%至24.96%。气相混合制冷剂的温度升高6.45℃,在复合气调和俯仰条件下,热交换减少37.90W。

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