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Modeling evaluation on solid-liquid mixing characteristics in a dislocated guide impeller stirred tank

  • Deyin Gu EMAIL logo , Fenghui Zhao , Xingmin Wang and Zuohua Liu
Published/Copyright: September 20, 2021

Abstract

The solid-liquid mixing characteristics in a stirred tank with pitched blade impellers, dislocated impellers, and dislocated guide impellers were investigated through using CFD simulation. The effects of impeller speed, impeller type, aperture ratio, aperture length, solid particle diameter and initial solid holdup on the homogeneity degree in the solid-liquid mixing process were investigated. As expected, the solid particle suspension quality was increased with an increase in impeller speed. The dislocated impeller could reduce the accumulation of solid particles and improve the cloud height compared with pitched blade impeller under the same power consumption. The dislocated guide impeller could enhance the solid particles suspension quality on the basis of dislocated impeller, and the optimum aperture ratio and aperture length of dislocated guide impeller were 12.25% and 7 mm, respectively, in the solid-liquid mixing process. Smaller solid particle diameter and lower initial solid holdup led to higher homogeneity degree of solid-liquid mixing system. The dislocated guide impeller could increase solid particle integrated velocity and enhance turbulent intensity of solid-liquid two-phase compared with pitched blade impeller and dislocated impeller under the same power consumption.


Corresponding author: Deyin Gu, School of Environment and Resources, Chongqing Technology and Business University, Chongqing 400060, China, E-mail:

Funding source: Science and Technology Research Project of Chongqing Education Commission

Award Identifier / Grant number: KJQN201900802

Funding source: Scientific Research Projects for High-Level Talents of Chongqing Technology and Business University

Award Identifier / Grant number: 1956006

Funding source: Natural Science Foundation of Chongqing Technology and Business University

Award Identifier / Grant number: 1952041

  1. Author contributions: Deyin Gu: conceptualization, methodology, software, investigation, formal analysis, supervision, writing-original draft. Fenghui Zhao: writing-review and editing. Xingmin Wang: writing-review and editing. Zuohua Liu: writing - review and editing.

  2. Research funding: The study was supported by the Science and Technology Research Project of Chongqing Education Commission (KJQN201900802), Scientific Research Projects for High-Level Talents of Chongqing Technology and Business University (1956006), and Natural Science Foundation of Chongqing Technology and Business University (1952041).

  3. Conflict of interest statement: The authors declare no conflicts of interest regarding this article.

Nomenclature

H

liquid height, m

T

stirred tank diameter, m

R

stirred tank radius, m

z

axial coordinate, m

r

radial coordinate, m

C h

local solid volume fraction at height of h in simulation

C avg

average solid volume fraction

n

number of sapling points

g

gravitational acceleration, m/s2

C ε1, C ε2, C μ

parameters in the standard k-ε model

k

turbulent kinetic energy, m2/s2

F drag

drag force, N

C D

drag coefficient

N

impeller speed, s−1

P

power consumption, W

ξ

homogeneity

ρ l

liquid density, kg/m3

ρ s

solid density, kg/m3

ρ

density, kg/m3

α

volume fraction

α l

liquid phase volume fraction

α s

solid phase volume fraction

ε

turbulent energy dissipation rate

μ

viscosity, Pa·s

μ l

liquid phase viscosity, Pa·s

μ t

turbulent viscosity, Pa·s

μ tl

liquid phase turbulent viscosity, Pa·s

σ k , σ ε

k and ε turbulent Prandtl number

ω

quality of the solid-liquid mixing system, kg

V

volume of the solid-liquid mixing system, m3

V s

solid phase volume of the solid-liquid mixing system, m3

C v

local solid volume fraction in experiment

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Received: 2021-05-31
Accepted: 2021-09-09
Published Online: 2021-09-20

© 2021 Walter de Gruyter GmbH, Berlin/Boston

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