An investigation on structural parameters optimization and coupled heat transfer of LNG submerged combustion vaporizer

被引:4
作者
Han, Changliang [3 ]
Huang, Yiyan
Chen, Zhipeng [1 ,2 ]
Wu, Yizhong
Bao, Shunyu [3 ]
Zhao, Fangwei [1 ,2 ]
Li, Xibing [1 ,2 ,4 ]
机构
[1] Fujian Agr & Forestry Univ, Coll Mech & Elect Engn, Fuzhou 350002, Peoples R China
[2] Fujian Agr & Forestry Univ, Fujian Key Lab Agr Informat Sensing Technol, Fuzhou 350002, Peoples R China
[3] Harbin Univ Sci & Technol, Sch Mech & Power Engn, Harbin 150080, Peoples R China
[4] Fujian Agr & Forestry Univ, Coll Mech & Elect Engn, 15 Shangxiadian Rd, Fuzhou 350002, Fujian, Peoples R China
关键词
Submerged combustion vaporizer; Structural parameters; Multi-parameter orthogonal combination; optimization; Coupled heat transfer; INTERMEDIATE FLUID VAPORIZER; THERMAL PERFORMANCE ANALYSIS; DESIGN; FLOW;
D O I
10.1016/j.cryogenics.2023.103764
中图分类号
O414.1 [热力学];
学科分类号
摘要
Submerged combustion vaporizer (SCV) owns an extremely efficient multiphase heat exchanger adopted in the coastal liquefied natural gas (LNG) receiving terminal. Overall vaporization efficiency of SCV mostly depends on the matching relationship of structural parameters and coupled heat transfer characteristics, which has been rarely addressed in previous studies. In the present work, an integrated SCV experimental platform with handling capacity of 50 kg/h was set up to validate the reliability of numerical model and method. Additionally, on ac-count of multi-parameter orthogonal combination optimization method, the effects and sensitivity orders of structural parameters (transverse tube pitch, longitudinal tube pitch, orifice size and number of distributor branch) on dynamics performance of SCV were investigated. Finally, the coupled heat transfer between gas-liquid two-phase flow and supercritical LNG gasification was revealed in view of optimized parameters. Results indicated that the transient numerical tube-side outlet temperature could be consistent with experimental data. For the shell-side heat transfer coefficient, the sensitivity order was transverse tube pitch > orifice size > longitudinal tube pitch > number of distributor branch. Nevertheless, for the shell-side pressure drop, the sensitivity order was longitudinal tube pitch > transverse tube pitch > orifice size > number of distributor branch. Under the condition of optimization scheme, the heat provided by gas-liquid two-phase flow could meet the requirements of supercritical LNG gasification, the NG outlet temperature might achieve approximately 272 K. The present outcomes could lay a foundation for the optimization design and deep understanding for actual SCV facility.
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页数:13
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