Design and Research of Three-Stage Reactor of Carbonation Process of Calcified Residue

被引:0
|
作者
Li, Xiang [1 ]
Liu, Yan [1 ]
Zhang, Tingan [1 ]
Xiao, Yadong [1 ]
Li, Xiaolong [1 ]
Wang, Kun [1 ]
Liu, Guanting [1 ]
机构
[1] Northeastern Univ, Sch Met, Shenyang 110819, Peoples R China
来源
ENERGY TECHNOLOGY 2024 | 2024年
基金
中国博士后科学基金;
关键词
Carbonization; Jet flow; Venturi; Absorption rate; Utilization rate; Physical simulation; BAYER RED MUD; RECOVERY; ALUMINA; BAUXITE; ALKALI;
D O I
10.1007/978-3-031-50244-6_19
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A three-stage cross-flow Venturi jet reactor was innovatively designed in this study to conduct an experimental study on the physical simulation of the carbonization process of calcified slag. The pH changes during CO2 absorption by NaOH were measured by a pH meter. The influence law of superficial gas velocity, superficial liquid velocity, and inlet pressure on CO2 absorption rate and utilization rate were investigated. The results show that the volumetric mass transfer coefficient with the increase of superficial gas velocity first remains unchanged and then increases, decreases with the increase of superficial liquid velocity, and increases with the increase of inlet pressure, and the latter stage is greater than the previous stage. The CO2 utilization rate does not change with the increase of superficial gas velocity and inlet liquid velocity but increases with the increase of inlet pressure and remains unchanged afterwards. This result provides support for the design and industrial application of carbonization reactors.
引用
收藏
页码:215 / 226
页数:12
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