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摘要:
Heat transfer and bubble phenomena were investigated by adopting the drift flux model in a viscous slurry bubble column reactor (SBCR), having a diameter of 0.0508 m(ID) and height 1.5 m. The effects of superficial gas velocity (0.002 -0.164 m/s), solid concentration (0 - 20 wt%) and liquid viscosity (paraffin oil;16.9 mPa•s and squalane;25.9 mPa•s) on the gas holdup and heat transfer characteristics were examined. It was observed that the gas holdup increased with increasing superficial gas velocity (UG), but decreased with increasing solid concentration (SC) or slurry viscosity. The degree of non-uniformity in a SBCR could be determined by the modified drift flux model at the heterogeneous flow regime. The local heat transfer coefficient (h) between the immersed heater and the bed decreased with increasing liquid viscosity and SC, but it increased with increasing UG. The modified Nusselt number including the gas holdup and local heat transfer coefficient was well correlated in terms of dimensionless groups such as Reynolds and Prandtl numbers.
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篇名 Bubble and Heat Transfer Phenomena in Viscous Slurry Bubble Column
来源期刊 化学工程与科学期刊(英文) 学科 物理学
关键词 Gas HOLDUP SLURRY BUBBLE COLUMN Heat Transfer DRIFT Flux Model
年,卷(期) 2014,(4) 所属期刊栏目
研究方向 页码范围 417-429
页数 13页 分类号 O3
字数 语种
DOI
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Gas
HOLDUP
SLURRY
BUBBLE
COLUMN
Heat
Transfer
DRIFT
Flux
Model
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期刊影响力
化学工程与科学期刊(英文)
季刊
2160-0392
武汉市江夏区汤逊湖北路38号光谷总部空间
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386
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0
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