FLOW CHARACTERISTICS NEAR THE NOZZLE IN A BUBBLE COLUMN WITH SIMULTANEOUS GAS-LIQUID INJECTION

被引：5

作者：

IDOGAWA, K

FUKUDA, T

NAGAISHI, H

MAEKAWA, Y

CHIBA, T

MOROOKA, S

机构：

[1] HOKKAIDO UNIV,MET CHEM RES INST,SAPPORO,HOKKAIDO 060,JAPAN

[2] KYUSHU UNIV,DEPT APPL CHEM,FUKUOKA 812,JAPAN

来源：

KAGAKU KOGAKU RONBUNSHU | 1990年 / 16卷 / 06期

关键词：

Bubble Column; Bubble Size; Bubble Velocity; Coal Liquefaction Reactor; Flow Properties; Gas Holdup; Optical Fiber Probe; Simultaneous Injection Nozzle;

D O I：

10.1252/kakoronbunshu.16.1210

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

Gas holdup, bubble rising velocity and bubble size were measured by an opticalfiber probe near a nozzle in a bubble column with simultaneous gas-liquid injection. A jet-like spouting stream was formed near the nozzle, and the height of the jet was not affected by the diameter of the nozzle. Bubbles were formed at the side wall and the top of the jet, and they dispersed radially with increasing axial position. When the axial position was greater than 88 cm from the nozzle, the radial distribution of gas holdup became uniform regardless of axial position. The radial dispersion and the bubble diameter depended on the nozzle diameter, and the effects of simultaneous gas-liquid injection on the bubble formation were similar to those of an increase of pressure. © 1990, The Society of Chemical Engineers, Japan. All rights reserved.

引用

页码：1210 / 1215

页数：6

共 50 条

[31] The effect of electrolyte concentration on counter-current gas-liquid bubble column fluid dynamics: Gas holdup, flow regime transition and bubble size distributions
Besagni, Giorgio
Inzoli, Fabio
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2017, 118 : 170 - 193
[32] Mixing in a gas/liquid flow countercurrent bubble column
Bartrand, TA
Farouk, B
Haas, CN
Computational Methods in Multiphase Flow III, 2005, 50 : 35 - 44
[33] Radial Profiles of Gas Bubble Behavior in a Gas-Liquid Bubble Column Reactor under Elevated Pressures
Jin, Haibo
Qin, Yujian
Yang, Suohe
He, Guangxiang
Guo, Zhiwu
CHEMICAL ENGINEERING & TECHNOLOGY, 2013, 36 (10) : 1721 - 1728
[34] Generality of CFD-PBM coupled model for simulations of gas-liquid bubble column
Zhang H.
Wang T.
Huagong Xuebao/CIESC Journal, 2019, 70 (02): : 487 - 495
[35] GAS-LIQUID MASS-TRANSFER IN A BUBBLE COLUMN WITH ORGANIC LIQUIDS
GRUND, G
SCHUMPE, A
DECKWER, WD
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (13-14) : 3509 - 3516
[36] Prediction of pressure drop in a modified gas-liquid downflow bubble column
Majumder, Subrata Kumar
Kundu, Gautam
Mukherjee, Dibyendu
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (12) : 4060 - 4070
[37] Effect of gas flow rate and nozzle diameter on bubble size and shape distributions in bubble column
Yan, Hong-jie
Zhang, He -yang
Liu, Liu
Ziegenhein, Thomas
Zhou, Ping
TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA, 2024, 34 (05) : 1710 - 1720
[38] Homogeneous and re-circulatory gas-liquid flow in a bubble column: A numerical investigation using OpenFOAM
Panda, Saroj K.
SN APPLIED SCIENCES, 2021, 3 (06):
[39] GAS ENTRAINMENT AND DEPTH OF PENETRATION IN A COCURRENT GAS-LIQUID DOWNFLOW BUBBLE-COLUMN
KUNDU, G
MUKHERJEE, D
MITRA, AK
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1994, 27 (05) : 621 - 626
[40] Comparative evaluation of hydrodynamic and gas-liquid mass transfer characteristics in bubble column and airlift slurry reactors
Choi, KH
Chisti, Y
MooYoung, M
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1996, 62 (03): : 223 - 229

← 1 2 3 4 5 →