曹学文, 吉俊毅, 杨文. LNG卸料管道氮气预冷温度分布规律[J]. 油气储运, 2016, 35(5): 492-497. DOI: 10.6047/j.issn.1000-8241.2016.05.008
引用本文: 曹学文, 吉俊毅, 杨文. LNG卸料管道氮气预冷温度分布规律[J]. 油气储运, 2016, 35(5): 492-497. DOI: 10.6047/j.issn.1000-8241.2016.05.008
CAO Xuewen, JI Junyi, YANG Wen. Temperature distribution of LNG unloading pipelines during nitrogen pre-cooling[J]. Oil & Gas Storage and Transportation, 2016, 35(5): 492-497. DOI: 10.6047/j.issn.1000-8241.2016.05.008
Citation: CAO Xuewen, JI Junyi, YANG Wen. Temperature distribution of LNG unloading pipelines during nitrogen pre-cooling[J]. Oil & Gas Storage and Transportation, 2016, 35(5): 492-497. DOI: 10.6047/j.issn.1000-8241.2016.05.008

LNG卸料管道氮气预冷温度分布规律

Temperature distribution of LNG unloading pipelines during nitrogen pre-cooling

  • 摘要: LNG进入常温卸料管道前需进行预冷, 在低温氮气预冷过程中, 会出现管道顶底温差较大的现象, 过大的顶底温差会造成管道拱起。利用Fluent软件, 建立LNG卸料管道氮气预冷三维模型, 采用阶段降低氮气入口温度的预冷方式, 模拟氮气预冷卸料管道温度分布规律, 探究卸料管道顶底温差产生原因及影响因素。结果表明: 在预冷过程中, 管道近管壁处温度梯度大, 管道内部温度梯度较小; 同时预冷过程中管道内自然对流作用不可忽略, 与管道换热后的氮气温度升高、密度减小, 在浮升力作用下向上运动, 从而导致顶部温度高于底部温度; 影响顶底温差大小的因素有预冷时间、质量流量、氮气温度等; 顶底温差随时间先增大后减小, 质量流量越大, 氮气入口温度越低, 管道顶底温差越大。为避免管道顶底温差过大和预冷速度不超过10 K/h, 建议采用阶梯式预冷建议逐渐将温度降至123 K左右。

     

    Abstract: LNG (liquefied natural gas) is usually pre-cooled before it flows into normal temperature unloading pipelines. In the process of low-temperature nitrogen pre-cooling, the temperature difference between the top and the bottom of the pipeline is large. If the temperature difference is too large, the pipeline will be upwarped. In this paper, a 3D nitrogen pre-cooling model for LNG unloading pipelines was established by using Fluent. Then, the temperature distribution of unloading pipelines during nitrogen pre-cooling was simulated by decreasing the inlet temperature of nitrogen step by step. And finally, a series of studies were performed on the causes and influence factors of top-bottom temperature difference of unloading pipelines. The results show that, during pre-cooling, the temperature gradient is higher near the pipe wall, but lower inside the pipeline. Attention shall be paid to the natural convection inside the pipeline during pre-cooling. After its heat exchange with the pipelines, the nitrogen rises in temperature and drops in density. Under the effect of buoyancy, the nitrogen flows upward. And consequently, the temperature at the top is higher than that at the bottom. The top-bottom temperature difference is influenced by the following factors, such as pre-cooling time, mass flow and nitrogen temperature. The temperature difference increases at first and then decreases. The larger the mass flow is and the lower the nitrogen inlet temperature is, the larger the temperature difference appears. In order to prevent the top-bottom temperature difference from rising too high and keep the pre-cooling rate below 10 K/h, the temperature is decreased gradually to 123 K by means of step pre-cooling.

     

/

返回文章
返回