scholarly journals Mass transfer in stirred tank for phenolic extraction from coal tar

2017 ◽  
Author(s):  
Dewi Selvia Fardhyanti ◽  
Bahy Wibowo ◽  
Muhammad Rafiqi
2017 ◽  
Vol 824 ◽  
pp. 012019
Author(s):  
D S Fardhyanti ◽  
D S Tyaningsih ◽  
S N Afifah

2019 ◽  
Vol 145 ◽  
pp. 314-322 ◽  
Author(s):  
Baoqing Liu ◽  
Qing Xiao ◽  
Ning Sun ◽  
Pengfei Gao ◽  
Fangyi Fan ◽  
...  

2021 ◽  
Vol 8 ◽  
pp. 100180
Author(s):  
S. Matthes ◽  
T. Merbach ◽  
J. Fitschen ◽  
M. Hoffmann ◽  
M. Schlüter

1997 ◽  
Vol 31 (8) ◽  
pp. 2268-2276 ◽  
Author(s):  
Anuradha Ramaswami ◽  
Subhasis Ghoshal ◽  
Richard G. Luthy
Keyword(s):  

Author(s):  
Lei Wang ◽  
Xiao Xu ◽  
Hualin Wang ◽  
HongLai Liu ◽  
Qiang Yang

A gas-liquid stirred tank reactor (STR) has some problems, such as low mass transfer efficiency, high exhaust gas oxygen concentration, and low product conversion rate, due to limitations of stirring speed and input power. This article proposes a method to enhance the gas-liquid mass transfer in a STR using circulating jet internals. When a circulating jet is added, the average bubble size in the reactor is reduced to 1.26 mm, and the overall gas holdup is increased to 8.23%, which is an increase of 3.62 times of the original STR. The gas-liquid volumetric mass transfer coefficient is increased to 0.05556 s-1, which is 4.84 times of the original STR. The unit volume power is increased by only 1.4 times. These data provide references for the design and scale-up of new jet STRs.


2016 ◽  
Vol 39 (5) ◽  
pp. 945-952 ◽  
Author(s):  
Xiangyang Li ◽  
Pingping Li ◽  
Liangzhu Zu ◽  
Chao Yang

1995 ◽  
pp. 142-149
Author(s):  
Subhasis Goshal ◽  
Anuradha Ramaswami ◽  
Richard G. Luthy
Keyword(s):  

Sign in / Sign up

Export Citation Format

Share Document