Secondary steam flow characteristics and heat transfer effects in a horizontal tube falling film evaporator based on CFD-distributed parameter model

IF 9.8 1区 工程技术 Q1 ENGINEERING, CHEMICAL
Chao Li, Luyuan Gong, Xingsen Mu, Yali Guo, Shengqiang Shen
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引用次数: 0

Abstract

This study establishes a three-dimensional Distributed Parameter(DP) model for a horizontal tube falling film evaporator(HTFFE) in a Low-Temperature Multi-effect Desalination (LT-MED) system. An innovative computational method integrating the DP model and Computational Fluid Dynamics methods is proposed, which fully couples the flow and heat transfer processes inside, outside, and between the tubes. This method effectively resolves the simulation problems in previous studies where secondary steam flow process were either uncalculable or oversimplified. Using an actual two-pass HTFFE as a case study, the model reveals distributions of inter-tube pressure, secondary steam velocity, and other thermal parameters. The concept of a “flow center” for secondary steam was defined, and it was found that over 70 % of the secondary steam exits through the side boundary of the tube bundle. The study clarifies the mechanism by which secondary steam influences evaporator performance: an increase in inter-tube pressure elevates the seawater temperature, which thereby reduces the effective heat transfer temperature difference(ΔTeff), leading to thermal parameter inhomogeneity along the tube bundle. The impact of secondary steam flow on ΔTeff was quantified under varying apparent heat transfer temperature differences(ΔTap) and total tube column numbers. It demonstrates a reduction in ΔTeff of up to 17.32 %, with a local loss reaching 56.04 % when combined with seawater boiling point elevation under certain conditions. Furthermore, local and overall relative change rate indicators of thermal parameters were defined. These indicators reflect that the location of the local ΔTeff loss occurs in the region near the heating steam outlet for each pass, while the secondary steam flow enhances the overall heat transfer coefficient but reduces both the average ΔTeff and the total water production.
基于cfd分布参数模型的水平管降膜蒸发器二次蒸汽流动特性及换热效果
建立了低温多效脱盐(LT-MED)系统中水平管降膜蒸发器(HTFFE)的三维分布参数(DP)模型。提出了一种将DP模型与计算流体力学方法相结合的计算方法,将管内、外、管间的流动和换热过程充分耦合。该方法有效地解决了以往研究中二次蒸汽流动过程难以计算或过于简化的模拟问题。该模型以实际的两道HTFFE为例,揭示了管间压力、二次蒸汽速度和其他热参数的分布。定义了二次蒸汽“流动中心”的概念,发现70%以上的二次蒸汽通过管束的侧边界出口。本研究阐明了二次蒸汽影响蒸发器性能的机理:管间压力的升高使海水温度升高,从而减小了有效换热温差(ΔTeff),导致沿管束的热参数不均匀性。在不同的表观换热温差(ΔTap)和总管柱数下,量化了二次蒸汽流量对ΔTeff的影响。在一定条件下,结合海水沸点海拔,ΔTeff降低幅度可达17.32%,局部损失达56.04%。此外,还定义了局部和整体热参数的相对变化率指标。这些指标反映了局部ΔTeff损失的位置发生在每道次加热蒸汽出口附近的区域,而二次蒸汽流提高了总体换热系数,但降低了平均ΔTeff和总产水量。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Desalination
Desalination 工程技术-工程:化工
CiteScore
14.60
自引率
20.20%
发文量
619
审稿时长
41 days
期刊介绍: Desalination is a scholarly journal that focuses on the field of desalination materials, processes, and associated technologies. It encompasses a wide range of disciplines and aims to publish exceptional papers in this area. The journal invites submissions that explicitly revolve around water desalting and its applications to various sources such as seawater, groundwater, and wastewater. It particularly encourages research on diverse desalination methods including thermal, membrane, sorption, and hybrid processes. By providing a platform for innovative studies, Desalination aims to advance the understanding and development of desalination technologies, promoting sustainable solutions for water scarcity challenges.
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