摘要
Experimental study was carried out of heat transfer of the Gas Carrying Evaportion with fluidized solid particles in a vertical annulus. The annulus consists of an electrical heating bar and an outer glass tube. Air was adopted as the carrying gas. Water and aqueous solutions of carboxyl methyl cellulose were used as the working liquids. Solid particles were ceramic beads and glass beads of different diameter. The experimental results showed that the liquid flow boiling heat transfer was increased and the superheat of liquid at heating surface lowered remarkably by the introduction of the carrying gas and the fluidized solid pericles. The heat transfer augmentation became weaker as the liquid viscosity icreased.Experimental data of the heat transfer were correlated.
Experimental study was carried out of heat transfer of the Gas Carrying Evaportion with fluidized solid particles in a vertical annulus. The annulus consists of an electrical heating bar and an outer glass tube. Air was adopted as the carrying gas. Water and aqueous solutions of carboxyl methyl cellulose were used as the working liquids. Solid particles were ceramic beads and glass beads of different diameter. The experimental results showed that the liquid flow boiling heat transfer was increased and the superheat of liquid at heating surface lowered remarkably by the introduction of the carrying gas and the fluidized solid pericles. The heat transfer augmentation became weaker as the liquid viscosity icreased.Experimental data of the heat transfer were correlated.
出处
《工程热物理学报》
EI
CAS
CSCD
北大核心
1998年第4期484-487,共4页
Journal of Engineering Thermophysics
基金
国家自然科学基金
关键词
蒸发
传热
三相流
自然循环
gas-liquid-solid three-phase, evaporation, heat transfer
