Liquid-liquid mass transfer in a serpentine miniature geometry- effect on pressure drop

被引：16

作者：

Prakash, Ravi ^{[1
]}

Verma, Raj Kumar ^{[1
]}

Ghosh, Sumana ^{[1
]}

机构：

[1] IIT Roorkee, Dept Chem Engn, Roorkee 247667, Uttar Pradesh, India

来源：

CHEMICAL ENGINEERING JOURNAL | 2019年 / 369卷

关键词：

Liquid-liquid flow; Pressure drop; Slug flow; Miniature reactor; Extraction; COILED FLOW INVERTER; SLUG FLOW; TAYLOR FLOW; EXTRACTION; INTENSIFICATION; MICROCHANNELS; CAPILLARY; DIAMETER; PATTERNS; SYSTEM;

D O I：

10.1016/j.cej.2019.03.064

中图分类号：

X [环境科学、安全科学];

学科分类号：

08 ; 0830 ;

摘要：

In this paper, extraction of acetic acid from toluene with water as solvent has been studied in a serpentine miniature geometry of circular cross section with 2 mm inner diameter. The results are further compared with that obtained in a straight tube of same inner diameter. It is observed that, serpentine geometry is responsible for formation of slug droplet regime instead of only slug regime as observed in straight tube. Also due to presence of secondary flow, mass transfer efficiency in serpentine geometry found to be 1.2 times higher than that in straight tube. This results in lower pressure drop than that observed in straight tube. The maximum extraction efficiency in serpentine geometry found to be 94% for the feed to solvent ratio 10.

引用

页码：489 / 497

页数：9

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