详细信息
Pressure drop and gas holdup in an upward-flow fixed-bed reactor ( SCI-EXPANDED收录 EI收录)
文献类型:期刊文献
英文题名:Pressure drop and gas holdup in an upward-flow fixed-bed reactor
作者:Song, Zhibo[1];Bi, Jinghao[2];Xu, Xiao[2];Yang, Qiang[2]
机构:[1]Sinopec Engn Inc, Beijing 100101, Peoples R China;[2]East China Univ Sci & Technol, Sch Mech & Power Engn, Shanghai 200237, Peoples R China
年份:2025
卷号:88
起止页码:42
外文期刊名:CHINESE JOURNAL OF CHEMICAL ENGINEERING
收录:;EI(收录号:20254919660723);WOS:【SCI-EXPANDED(收录号:WOS:001691430500001)】;
基金:This work is financially supported by the National Natural Science Foundation of China (52025103) .
语种:英文
外文关键词:Fixed-bed reactor; Pressure drop; Gas holdup; Bubble characteristics
摘要:This study presents a systematic investigation of pressure drop and gas holdup in an upward-flow fixed-bed reactor, examining the effects of bubble size, bed height, particle shape, superficial gas velocity (SGV), and superficial liquid velocity (SLV) based on experimental measurements and empirical correlations. Two bubble generators, namely ring tube generator (RTG) and porous sintered film generator (PSG), are used. Key findings reveal that for the PSG, increasing SGV decreases small-bubble population while promoting large-bubble formation, with the bubbles stabilizing at a Sauter mean diameter (d(32)) of similar to 3 mm. The RTG produces stable large bubbles (d(32) = 6-7 mm) with minimal size variations across the range of tested SGVs. The pressure drop decreases with an increase in SGV but increases with higher SLV and bed height, primarily due to the reduced liquid holdup and the dominance of static pressure. Smaller bubbles reduce the pressure drop by slowing rise velocity and minimizing frictional resistance. Clover-shaped particles exhibit the highest pressure drop owing to large porosity, while 3-mm toothed spheres show higher pressure drop than 5-mm spheres at high SGV because of intensified capillary forces. The gas holdup increases with increasing SGV and bed height but decreases slightly with increasing SLV. Smaller bubbles enhance gas holdup by improving bed distribution and residence time. The 3-mm toothed spheres show the highest gas holdup due to stronger capillary trapping, whereas the clover-shaped particles exhibit the lowest. Empirical correlations for pressure drop and gas holdup are developed, yielding calculation errors within +/- 1% and +/- 20% of the experimental values, respectively. (c) 2025 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd. All rights are reserved, including those for text and data mining, AI training, and similar technologies.
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