Effects of blade structures on the dissolution and gas-liquid mass transfer performance of cup-shaped blade mixers

被引:13
作者
Dang, Xiuhu [1 ]
Guo, Junheng [1 ]
Yang, Lin [1 ]
Xue, Song [1 ]
Ai, Bingyan [1 ]
Li, Xiaoning [1 ]
Chen, Liying [1 ]
Li, Wei [1 ]
Qin, Hongyun [2 ]
Zhang, Jinli [1 ,3 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Tianjin 300350, Peoples R China
[2] Shandong Univ Technol, Sch Chem & Chem Engn, Zibo 255000, Peoples R China
[3] Shihezi Univ, Sch Chem & Chem Engn, Shihezi 832003, Peoples R China
基金
中国国家自然科学基金;
关键词
Cup-shaped blade mixer; Solid-liquid mass transfer; Dissolution; Gas-liquid mass transfer; TRANSFER COEFFICIENT; PITCHED BLADE; MIXING TIME; HOLD-UP; IMPELLER; CONFIGURATIONS; TURBINE; PATTERN;
D O I
10.1016/j.jtice.2021.11.016
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Background: A mixer with the advantages of excellent mixing performance and easy manufacturing is widely needed in industrial applications. In this work, the solid-liquid and gas-liquid mass transfer characteristics of a cup-shaped blade mixer, which is obtained by cutting a 90 degrees stainless-steel elbow, are investigated. Methods: The effects of blade structure, blade angle, blade height, baffle presence, surface tension, and gas holding on mass transfer characteristics were investigated by the conductivity probe and the dissolved oxygen dynamic method. Significant findings: Results show that the solid-liquid and gas-liquid mass transfer performance is enhanced as the inlet area of the cup-shaped blade is increased and the optimum blade angles are 22.5 degrees and 15 degrees respectively. The solid-liquid mass transfer performance can be improved when the baffles are removed. The gasliquid mass transfer performance first deteriorates but then improves as the surfactant concentration is increased. Moreover, the mass transfer performance of the cup-shaped blade mixer is superior to that of the 45 degrees -pitched blade and Rushton turbine. Meanwhile, the correlations of the solid-liquid and gas-liquid mass transfer coefficients are obtained, which would provide insight for the industrial design, optimization, and scale-up of cup-shaped blade mixers for multiphase systems. (C) 2021 Taiwan Institute of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
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页数:10
相关论文
共 35 条
[21]   Gas hold-up, mixing time and gas-liquid volumetric mass transfer coefficient of various multiple-impeller configurations:: Rushton turbine, pitched blade and techmix impeller and their combinations [J].
Moucha, T ;
Linek, V ;
Prokopová, E .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (09) :1839-1846
[22]   EFFECT OF IMPELLER-TANK CONFIGURATIONS ON FLUID-PARTICLE MASS-TRANSFER [J].
NIENOW, AW ;
MILES, D .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1978, 15 (01) :13-24
[23]   SOLID DISTRIBUTION AND MIXING TIME IN STIRRED TANKS: THE CASE OF FLOATING PARTICLES [J].
Paglianti, Alessandro ;
Carletti, Claudio ;
Busciglio, Antonio ;
Montante, Giuseppina .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2017, 95 (09) :1789-1799
[24]   Particle-liquid mass transfer coefficient in two-/three-phase stirred tank reactors [J].
Pangarkar, VG ;
Yawalkar, AA ;
Sharma, MM ;
Beenackers, AACM .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (17) :4141-4167
[25]   Impact of HSPBT blade angle on gas phase hydrodynamics in a gas-liquid stirred tank [J].
Prakash, Baranivignesh ;
Shah, Milinkumar T. ;
Pareek, Vishnu K. ;
Utikar, Ranjeet P. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2018, 130 :219-229
[26]   Gas-liquid mass transfer studies with triple impeller system on a laboratory scale bioreactor [J].
Puthli, MS ;
Rathod, VK ;
Pandit, AB .
BIOCHEMICAL ENGINEERING JOURNAL, 2005, 23 (01) :25-30
[27]  
Raheem A, J TAIWAN INST CHEM E
[28]   Gas-Liquid Mass Transfer Characteristics in Two Inline High Shear Mixers [J].
Shi, Jintao ;
Xu, Shuangqing ;
Qin, Hongyun ;
Li, Wei ;
Zhang, Jinli .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (12) :4894-4901
[29]   Solid/liquid Mass Transfer Correlated to Mixing Pattern in a Mechanically-stirred Vessel [J].
Shiba, Ryutaro ;
Uddin, Md Azhar ;
Kato, Yoshiei ;
Kitamura, Shin-ya .
ISIJ INTERNATIONAL, 2014, 54 (12) :2754-2760
[30]   Enhancing Impeller Power Efficiency and Solid-Liquid Mass Transfer in an Agitated Vessel with Dual Impellers through Process Intensification [J].
Stoian, Daniel ;
Eshtiaghi, Nicky ;
Wu, Jie ;
Parthasarathy, Rajarathinam .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2017, 56 (24) :7021-7036