CFD gas–liquid simulation of oriented valve tray

2015 ◽  
Vol 23 (10) ◽  
pp. 1603-1609 ◽  
Author(s):  
Yufeng Ma ◽  
Lijun Ji ◽  
Jiexu Zhang ◽  
Kui Chen ◽  
Bin Wu ◽  
...  
Keyword(s):  
1973 ◽  
pp. 163-202 ◽  
Author(s):  
J.R. BACKHURST ◽  
J.H. HARKER
Keyword(s):  

2015 ◽  
Vol 9 (7) ◽  
pp. 148
Author(s):  
Fadlilatul Taufany ◽  
Nonot Soewarno ◽  
Melvina Eliana Sutanto ◽  
Indi Raisa Girsang

For the separation process in liquid-liquid mixture such as ethanol-water mixture, a sieve tray distillation columnis an alternatif for affordable process and maintenance. However to date, this sieve tray system is still currentlyhaving a lower Murphee efficiency and smaller interfacial area, as compared to other tray system, that is, either abubble cap or valve tray. Therefore it is of important to optimize the performance of sieve tray distillation bymeans of adding the wire mesh packing on that tray, as being the aim of the present study. This study isconducted by using a batch sieve tray distillation system, where the wire mesh packing is added on the third traythat is calculated from the top of the column, to avoid flooding inside the column. Here the resulting fermentedmolasses of containing a 10% volume of ethanol is used as a mixture distillation feed. The height of the wiremesh packing being studied is varied as 5 cm, 3 cm, and 2 cm. Our results showed that the Murphee efficiencyobtained by the variation of the packing height of 5 cm, 3 cm, 2 cm and without packing were 73.5%, 66.27%,56.86%, and 46.7% respectively, and were increased by subsequent level of the packing height. Thecorresponding hydrodynamic properties of this appended packing sieve tray distillation by means of theinterfacial area were 11.88 cm2/cm3, 0.48 cm2/cm3, and 0.32 cm2/cm3, while its pressure drop measured from thewater manometer height were 38.33 cm H2O/m, 30 cm H2O/m, 10 cm H2O/m for the packing height of 5 cm, 3cm, 2 cm height, respectively. The increasing of the performance of appended packing sieve tray distillation bymeans of the Murphee efficiency is explained by the increasing of the interfacial area for vapour-liquid than thetray itself. This preliminary study is expected to be a pioneer study of strategy to increase the performance ofconventional sieve tray distillation that is known as a kind of affordable distillation process.


2013 ◽  
Vol 21 (8) ◽  
pp. 821-826 ◽  
Author(s):  
Lühong ZHANG ◽  
Xuekuan LIU ◽  
Xingang LI ◽  
Xin GAO ◽  
Hong SUI ◽  
...  

2012 ◽  
Vol 443-444 ◽  
pp. 905-910
Author(s):  
Jie Xu Zhang ◽  
Cheng Fang Zhang

To increase the efficiency of float valve tray in plate column, a combined directed valve tray was developed. Comparative analysis of tray pressure drops, entrainments, weeping rates and mass transfers was conducted between the widely used V1-type float valve trays and the combined directed valve tray. The applications of the combined directed valve tray in atmospheric pressure device, catalytic cracking unit and gas fractionation device were also listed, which indicated that it was a significant improvement of float valve tray.


1984 ◽  
Vol 20 (3) ◽  
pp. 130-131
Author(s):  
M. N. Minnullin ◽  
G. G. Telyashev ◽  
R. R. Vakhitova ◽  
L. S. Pozin

1977 ◽  
Vol 16 (1) ◽  
pp. 79-82 ◽  
Author(s):  
Gavin R. Garrett ◽  
Robert H. Anderson ◽  
Matthew Van Winkle
Keyword(s):  
Scale Up ◽  

2013 ◽  
Vol 91 (6) ◽  
pp. 970-976 ◽  
Author(s):  
Qunsheng Li ◽  
Manxia Zhang ◽  
Xiaofei Tang ◽  
Lun Li ◽  
Zhigang Lei
Keyword(s):  

2015 ◽  
Author(s):  
Siti Nurkhamidah ◽  
Ali Altway ◽  
Ayu Savitri Wulansari ◽  
Evi Fitriyah Khanifah

2015 ◽  
Vol 126 ◽  
pp. 517-528 ◽  
Author(s):  
Rim Brahem ◽  
Aude Royon-Lebeaud ◽  
Dominique Legendre

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