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浸没燃烧式气化器换热管内跨临界液化天然气的传热特性

董文平 任婧杰 韩昌亮 杜丹 毕明树

化工进展2017,Vol.36Issue(12):4378-4384,7.
化工进展2017,Vol.36Issue(12):4378-4384,7.DOI:10.16085/j.issn.1000-6613.2017-0656

浸没燃烧式气化器换热管内跨临界液化天然气的传热特性

Heat transfer characteristic oftrans-critical liquefied natural gas on tube-side of submerged combustion vaporizer

董文平 1任婧杰 1韩昌亮 1杜丹 1毕明树1

作者信息

  • 1. 大连理工大学化工机械与安全学院,辽宁大连 116024
  • 折叠

摘要

Abstract

The thermal resistance of submerged combustion vaporizer(SCV)mainly locates inside the heat transfer tube. The study on the heat transfer characteristic oftrans-critical liquefied natural gas (LNG)is of great significance to improve the whole heat transfer efficiency of SCV. Therefore, numerical model was developed to describe the flow and heat transfer process oftrans-critical LNG in the tube. The heat transfer law oftrans-critical LNG in the tube was analyzed. And the effects of inlet velocity,inlet pressure and heat flux on the heat transfer behaviors were obtained. A new non-dimensional correlation was proposed,which was suitable to predict the heat transfer characteristics oftrans-critical LNG. Results showed that the local heat transfer coefficient firstly increases and then decreases,and the maximum value appears in the vicinity of the pseudo-critical temperature. The thermo-physical properties oftrans-critical LNG play a vital role in heat transfer enhancement. The local heat transfer coefficient is enhanced with the increase of inlet velocity. The maximum local heat transfer coefficient depends on the inlet pressure within limits. As the heat flux increases,the maximum local heat transfer coefficient appears earlier. The mean absolute percent error of the proposed non-dimensional heat transfer correlation is 6.53%. 99.42% of the data fall within the error zone of ±25%. The study can provide theoretical guidance for the design and economical operation of SCV.

关键词

浸没燃烧式气化器/跨临界液化天然气/传热/数值模拟

Key words

submerged combustion vaporizer/trans-critical LNG/heat transfer/numerical simulation

分类

能源科技

引用本文复制引用

董文平,任婧杰,韩昌亮,杜丹,毕明树..浸没燃烧式气化器换热管内跨临界液化天然气的传热特性[J].化工进展,2017,36(12):4378-4384,7.

基金项目

中央高校基本科研业务费专项资金资项目(DUT16QY29). (DUT16QY29)

化工进展

OA北大核心CSCDCSTPCD

1000-6613

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