The theoretical analysis on bubble mass transfer process was made by the non reversible thermodynamics. Non steady state, steady state and equilibrium state and changing regulation were discussed.
运用不可逆热力学原理，对气泡传质过程进行了理论分析，讨论了非稳态、稳态、平衡态的差异及其变化规律。
The mass transfer force concept was used to develop a model for the heat and mass transfer from a single superheated bubble rising in the water pool.
该文从传质推动力角度出发建立了高温气泡在水中上升过程的传热传质模型，计算结果与文献报道的实验数据、模拟结果基本吻合。
Several classical models for the gas-liquid mass transfer coefficient were compared, and the influences of the bubble size distribution and bubble wake effect were discussed.
比较了几种气液传质模型，讨论了气泡大小分布和气泡尾涡加速效应对气液传质的影响。
The characteristic of gas-liquid mass transfer in slurry bubble column reactor(SBCR) is reviewed.
本文总结了有关浆态鼓泡床反应器气液传质特性的研究成果。
A new model for mass transfer of air bubble in water is established.
建立了气泡传质的新的数学模型。
The influence of Taylor bubble movement on heat mass transfer was assumed based on the above analyses.
对上升管中气弹运动对传热传质的影响提出了假设。
The influence of Taylor bubble movement on heat mass transfer was assumed based on the above analyses.
对上升管中气弹运动对传热传质的影响提出了假设。
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