Effect of the thermal insulation layer on non-equilibrium condensation in the nozzle for carbon capture

IF 3.9 3区 工程技术 Q3 ENERGY & FUELS Chemical Engineering and Processing - Process Intensification Pub Date : 2025-02-01 Epub Date: 2024-12-07 DOI:10.1016/j.cep.2024.110124
Xiaoyang Han, Tongsheng Wang, Zhiheng Wang, Jianan Chen, Zhu Huang
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Abstract

A non-equilibrium phase transition model, grounded in the classical theory of droplet nucleation and growth, is constructed for the prediction of condensation phenomena in supersonic flows by coupling transport equations with source terms. The study investigates the influence of nozzle insulation on the spontaneous condensation of CO2. Results show that the maximum supercooling in the non-insulated model is 6.3% higher than in the insulated model, which leads to earlier nucleation of gas in the non-insulated model. To investigate the impact of the condensation model on the gas expansion, a comparison is conducted between a single-phase flow model and a condensation flow model. The results indicate that the single-phase flow model neglects the latent heat released during condensation, leading to an overestimation of the flue gas expansion capacity inside the nozzle. The maximum deviation of the Mach number between the two models reaches 13%. Increasing inlet saturation from 0.172 to 0.222 results in a forward shift of the Wilson point and a decrease in the maximum nucleation rate from 1.3 × 1022 m-3s-1 to 5.2 × 1021 m-3s-1. However, the increase in saturation favors gas liquefaction, leading to a 34% increase in the maximum liquid fraction, from 0.065 to 0.087.

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保温层对碳捕集喷嘴非平衡冷凝的影响
在经典液滴成核和生长理论的基础上,建立了一个非平衡相变模型,通过耦合输运方程和源项来预测超声速流动中的凝结现象。研究了喷嘴保温对CO2自发冷凝的影响。结果表明,非绝缘模型的最大过冷度比绝缘模型高6.3%,这导致非绝缘模型的气体更早成核。为了研究冷凝模型对气体膨胀的影响,对单相流模型和冷凝流模型进行了比较。结果表明,单相流模型忽略了冷凝过程中释放的潜热,导致对喷嘴内烟气膨胀能力的高估。两种型号的马赫数最大偏差达到13%。入口饱和度从0.172增加到0.222,导致威尔逊点前移,最大成核速率从1.3 × 1022 m-3s-1降低到5.2 × 1021 m-3s-1。然而,饱和度的增加有利于天然气液化,导致最大液体分数增加34%,从0.065增加到0.087。
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来源期刊
CiteScore
7.80
自引率
9.30%
发文量
408
审稿时长
49 days
期刊介绍: Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.
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