Characteristics of red mud slurry flow in carbonation reactor

被引:20
作者
Li, Ruibing [1 ,2 ]
Zhang, Ting'an [1 ]
Liu, Yan [1 ]
Zhou, Jianpeng [1 ]
Zou, Ruiping [2 ]
Kuang, Shibo [2 ]
机构
[1] Northeastern Univ, Sch Mat & Met, Shenyang 110819, Peoples R China
[2] Monash Univ, Dept Chem Engn, Lab Simulat & Modelling Particulate Syst, Clayton, Vic 3800, Australia
基金
中国国家自然科学基金;
关键词
Venturi reactor; Sauter diameter; Gas holdup; Mixing time; Mass transfer coefficient; GAS HOLD-UP; BUBBLE-COLUMNS; PRESSURE; TIME; BED;
D O I
10.1016/j.powtec.2016.11.028
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A new calcification-carbonation method was developed for treating bauxite residue (red mud), and a novel Venturi carbonation reactor (jet-flow reactor) was designed and used to process the bauxite residue. The characteristics of the fluid of gas-liquid and red mud slurry-gas-liquid phases in the jet flow reactor were investigated, mainly the effects of superficial gas and liquid velocities and the effective height-to-diameter ratio (H/D) of the reactor for gas holdup, mixing time, bubble refining, and CO2 absorption. The results show that the maximum CO2 utilization rate (eta) was achieved, i.e.eta = 833% when the H/D value of the reactor was 4 and superficial gas and liquid velocities were 10.62 m.s(-1) and 0.89 m.s(-1), respectively. The results provide a theoretical basis for the optimization of a new type of jet flow reactor. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:66 / 76
页数:11
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