Destruction of Trichloroethylene in a Two Stage Molten Salt Oxidation Reactor System

2008 ◽  
Vol 41 (7) ◽  
pp. 597-601 ◽  
Author(s):  
Hee-Chul Yang ◽  
Yong-Zun Cho ◽  
Hee-Chul Eun ◽  
Yong Kang
2007 ◽  
Vol 62 (18-20) ◽  
pp. 5137-5143 ◽  
Author(s):  
Hee-Chul Yang ◽  
Yong-June Cho ◽  
Hee-Chul Eun ◽  
Eung-Ho Kim

Chemosphere ◽  
2008 ◽  
Vol 73 (1) ◽  
pp. S311-S315 ◽  
Author(s):  
Hee-Chul Yang ◽  
Yong-Jun Cho ◽  
Hee-Chul Eun ◽  
Eung-Ho Kim

2010 ◽  
Vol 22 (2) ◽  
pp. 230-236 ◽  
Author(s):  
Rohan Jain ◽  
Ashish Pathak ◽  
T.R. Sreekrishnan ◽  
M.G. Dastidar

2020 ◽  
Vol 141 ◽  
pp. 107321 ◽  
Author(s):  
Fahad Alsayyari ◽  
Marco Tiberga ◽  
Zoltán Perkó ◽  
Danny Lathouwers ◽  
Jan Leen Kloosterman

AIChE Journal ◽  
1964 ◽  
Vol 10 (6) ◽  
pp. 944-951
Author(s):  
Robert D. Thibodeau ◽  
William F. Stevens

2014 ◽  
Vol 955-959 ◽  
pp. 2374-2377
Author(s):  
Chun Juan Dong ◽  
Tian Tian Zhao ◽  
Qing Ye Pan

To investigate the possibility of simultaneous high efficient removal of COD and NH3-N in the actual coking wastewater through micro-aerobic granular bio-film reactor, two-stage granular bio-film reactor system (EGSBI+ EGSBII) were continuously operated through two effluent recirculation ways for about 5 months: ERW1(24L.h-1 self-recirculation) and ERW2(15 L.h-1 self-recirculation +15 L.h-1 crossed recirculation). Compared with ERW1, through using ERW2, the two-stage EGSB reactor system could attain high COD and NH3-N removal efficiencies (86.7%-96.9% and 48.6%-80.4%) and low effluent NO2- and NO3- concentrations (0-25mg.L-1 and 7-71mg.L-1). Using ERW1, the two-stage EGSB reactor system melt with difficult of NO2- accumulation in the EGSBII (accompanied with low NH3-N removal of only 41.4%). Using ERW2, the difficult of accumulation in the EGSBII was solved and simultaneously high efficient removal of NH3-N and NO2- in the EGSBI was achieved.


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