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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2022, Vol. 16 Issue (4): 546-559   https://doi.org/10.1007/s11705-021-2069-3
  本期目录
Micromixing performance of the teethed high shear mixer under semi-batch operation
Xiaoning Li1, Lin Yang1, Junheng Guo1, Wei Li1, Mingliang Zhou2(), Jinli Zhang1,3()
1. School of Chemical Engineering and Technology, Tianjin University, Tianjin 300350, China
2. Department of Geotechnical Engineering, Tongji University, Shanghai 200092, China
3. School of Chemistry and Chemical Engineering, Shihezi University, Shihezi 832003, China
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Abstract

Semi-batch operated reaction processes are necessary for some competitive reaction systems to achieve a desirable process selectivity and productivity of fine chemical products. Herein the structural and operating parameters of the teethed high shear mixers were adjusted to study the micromixing performance in the semi-batch operated system, using the Villermaux/Dushman reaction system. The results indicate that the rising of the rotor speed and the number of rotor teeth, the decrease of the width of the shear gap and the radial distance between the feed position and the inner wall of stator can enhance the micromixing level and lead to the decrease of the segregation index. Additionally, computational fluid dynamics calculations were carried out to disclose the evolution of the flow pattern and turbulent energy dissipation rate of the semi-batch operated high shear mixer. Furthermore, the correlation was established with a mean relative error of 8.05% and R2 of 0.955 to fit the segregation index and the parameters studied in this work, which can provide valuable guidance on the design and optimization of the semi-batch operated high shear mixers in practical applications.

Key wordshigh shear mixer    semi-batch operation    micromixing performance    Villermaux/Dushman system    segregation index
收稿日期: 2021-03-02      出版日期: 2022-03-21
Corresponding Author(s): Mingliang Zhou,Jinli Zhang   
 引用本文:   
. [J]. Frontiers of Chemical Science and Engineering, 2022, 16(4): 546-559.
Xiaoning Li, Lin Yang, Junheng Guo, Wei Li, Mingliang Zhou, Jinli Zhang. Micromixing performance of the teethed high shear mixer under semi-batch operation. Front. Chem. Sci. Eng., 2022, 16(4): 546-559.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-021-2069-3
https://academic.hep.com.cn/fcse/CN/Y2022/V16/I4/546
Fig.1  
Parameter Rotor Stator Tank
Di/mm Φ12.5 Φ20 Φ70
Do/mm Φ18, Φ18.5, Φ19 Φ25 Φ75
Teeth gap/mm 2.5 2.0
Teeth number 2, 3, 6 12
Teeth height/mm 8, 11, 14 12
Tab.1  
Solution Compound Concentration/(mol·L–1)
Solution A H3BO3 0.1818
NaOH 0.0909
KI 0.0117
KIO3 0.0023
Solution B H2SO4 0.25, 0.5, 1.0
Tab.2  
Fig.2  
Fig.3  
Item Cells ε¯Body1/(m2·s–3) P/W
Mesh (1) 1.51 million 130.99 6.20
Mesh (2) 3.66 million 138.77 6.49
Mesh (3) 5.43 million 144.16 6.88
Mesh (4) 6.51 million 144.41 6.86
Tab.3  
Fig.4  
N/(r·min–1) Q/(mL·min–1)
3000 1.5
4500 1.5
6000 5
9000 8
12000 12
Tab.4  
Fig.5  
Fig.6  
Fig.7  
Fig.8  
Fig.9  
Reactor Operating conditions Viscosity/(Pa·s) Tip velocity/(m·s–1) Xs
Stirred reactor [7] VA = 1.0 L, VB = 4 mL,
[H+] = 1 mol·L–1
1.01 × 10−3 0.34–1.72 0.1466–0.2695
Stirred tank using RT [9] VA = 24.9 L, VB = 40 mL,
[H+] = 1 mol·L–1
1.01 × 10−3 1.52–2.79 0.0514–0.0720
Stirred tank using MRT [44] VA = 24.9 L, VB = 100 mL,
[H+] = 1 mol·L–1
1.01 × 10−3 1.51–2.77 0.0303–0.0552
Torus reactor [10] VA = 2.1 L, VB = 4.2 mL,
[H+] = 2 mol·L–1
1.01 × 10−3 0.46–2.73 0.1706–0.5038
Stirred tank with LDB [30] VA≈ 47.4 L, VB = 32 mL,
[H+] = 2 mol·L–1
0.80 0.28–1.40 0.0710–0.3350
HSM-6-0.5-8 (this study) VA = 0.5 L, VB = 6 mL,
[H+] = 1 mol·L–1
1.01 × 10−3 2.98–11.94 0.0085–0.0189
VA = 0.5 L, VB = 3 mL,
[H+] = 2 mol·L–1
1.01 × 10−3 2.98–11.94 0.0184–0.0346
Tab.5  
Fig.10  
Ref. Operation mode Chemical probe tm/s
[49] Inline Precipitation of boehmite and NH4-dawsonite 10−3
[18] Inline Villermaux/Dushman reaction 10−5
[27] Inline Villermaux/Dushman reaction 10−4
[41] Inline Diazo-coupling test reactions 10−4
This work Semi-batch Villermaux/Dushman reaction 10−4
Tab.6  
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