首页|LNG汽化器换热管内螺旋线圈传热性能强化研究

LNG汽化器换热管内螺旋线圈传热性能强化研究

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建立了 LNG汽化器换热管内的流动传热模型,研究LNG与蒸气换热的传热特点.模拟结果显示由于换热温差过大,采用光管换热管会发生管内膜态沸腾,无法实现LNG的高效汽化.提出在换热管内添加螺旋线圈内插件抑制膜态沸腾,换热性能提升可达77.1%,出口温度可达230.1 K,能够满足LNG汽化器的技术指标.对螺旋线圈的结构尺寸进行对比分析.线径从1 mm增至1.4 mm能提升换热效率并且不增加压降,而将节距从10 mm增值15 mm会导致流动传热性能恶化.
Study on heat transfer enhancement of wire coil insert in tube of LNG vaporizer
A flow and heat transfer model in the tube of an LNG vaporizer is established to in-vestigate the characteristics of LNG heat exchange with steam.The results show that the applica-tion of a plane tube will result in in-tube film boiling,which cannot ensure the vaporization of LNG due to the excessive heat transfer temperature difference.It is proposed to add a wire coil in-sert in the heat exchanger tube to inhibit film boiling,the heat transfer performance of which can be improved up to 77.1%.The outlet temperature of the tube can be up to 230.1 K,which can satisfy the technical specifications of the LNG vaporizer.The size effect of of wire coil insert is al-so analyzed.Increasing the wire diameter from 1 mm to 1.4 mm improves the heat transfer effi-ciency without increasing the pressure drop,while increasing the pitch from 10 mm to 15 mm re-sults in deterioration of the flow and heat transfer performance.

heat exchangerLNGheat transfer enhancement

顾陈杰、徐建浩、王健、邵雪锋

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中国船舶集团有限公司第七一一研究所 上海 201203

上海齐耀动力技术有限公司 上海 201203

换热器 LNG 传热强化

工信部高技术船舶科研项目

CBG3 N21-2-5

2024

低温工程
北京航天试验技术研究所

低温工程

CSTPCD北大核心
影响因子:0.568
ISSN:1000-6516
年,卷(期):2024.(1)
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