Boiling on Surfaces with Artificial Nucleation Sites( I ) Effect of Cavity Size and Cavity Density onBubble Diameter and Frequency ofDeparture in Pool Boiling
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Boiling on Surfaces with Artificial Nucleation Sites( I ) Effect of Cavity Size and Cavity Density onBubble Diameter and Frequency ofDeparture in Pool Boiling
CIESC JournalIssue 3, (1986)
作者机构:
大连工学院化学工程系,大连工学院化学工程系,大连工学院化学工程系
作者简介:
基金信息:
DOI:
CLC:
Online First:25 September 1986,
Published:25 September 1986
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陈嘉宾, 蔡振业, 林纪方. Boiling on Surfaces with Artificial Nucleation Sites( I ) Effect of Cavity Size and Cavity Density onBubble Diameter and Frequency ofDeparture in Pool Boiling[J]. CIESC Journal, 1986, (3).
DOI:
陈嘉宾, 蔡振业, 林纪方. Boiling on Surfaces with Artificial Nucleation Sites( I ) Effect of Cavity Size and Cavity Density onBubble Diameter and Frequency ofDeparture in Pool Boiling[J]. CIESC Journal, 1986, (3).DOI:
Boiling on Surfaces with Artificial Nucleation Sites( I ) Effect of Cavity Size and Cavity Density onBubble Diameter and Frequency ofDeparture in Pool Boiling
The effect of cavity size and cavity density on surfaces with artificial nucleation sites
on bubble diameter and trequency of departure in pool nucleate boiling was studied by using high-speed photography and laser fiber probe. A theoretical model has been developed from the analysis of force equilibrium of a bubble on a nucleation site with dueconsideration of the mutual influence of the surrounding bubbles. Preducted results obtained from the proposed model agree satisfactorily withexperimental data.
Analysis of flow field characteristics and mixing performance of different SK-type static mixers
Controlled synthesis of Bi2MoO6/MoO3 composite fibers via in-situ hydrothermal method and their high-efficiency photocatalytic hydrogen production performance
Zn-doped PdO/ZrO2 with rich oxygen vacancies for the synthesis of diphenyl carbonate from CO2 and phenol
Study on the residence time distribution characteristics of the TPMS-Diamond static mixer
Optimization of heat storage and release cycle performance of Ca(OH)2/CaO indirect reactor