Biological treatment of textile dye Acid violet-17 by bacterial consortium in an up-flow immobilized cell bioreactor

2004 ◽  
Vol 38 (5) ◽  
pp. 345-350 ◽  
Author(s):  
D.K. Sharma ◽  
H.S. Saini ◽  
M. Singh ◽  
S.S. Chimni ◽  
B.S. Chadha
2012 ◽  
Vol 2012 (10) ◽  
pp. 5540-5555
Author(s):  
Yakup Nurdogan ◽  
Craig A. Myler ◽  
George D. Lecakes ◽  
Paul J. Usinowicz ◽  
Eric P. Blumenstein

2004 ◽  
Vol 20 (4) ◽  
pp. 431-434 ◽  
Author(s):  
Deepak Kumar Sharma ◽  
Harvinder Singh Saini ◽  
Manjinder Singh ◽  
Swapandeep Singh Chimni ◽  
Bhupinder Singh Chadha

2004 ◽  
Vol 31 (3) ◽  
pp. 109-114 ◽  
Author(s):  
D. K. Sharma ◽  
H. S. Saini ◽  
M. Singh ◽  
S. S. Chimni ◽  
B. S. Chadha

Chemosphere ◽  
2021 ◽  
Vol 271 ◽  
pp. 129804
Author(s):  
Oscar M. Cornejo ◽  
Mariela Ortiz ◽  
Zaira G. Aguilar ◽  
José L. Nava
Keyword(s):  

2013 ◽  
Vol 30 (11) ◽  
pp. 2052-2058 ◽  
Author(s):  
Hajar Jamshidian ◽  
Seyyedhadi Khatami ◽  
Azadeh Mogharei ◽  
Farzaneh Vahabzadeha ◽  
Arvin Nickzad

2013 ◽  
Vol 145 ◽  
pp. 313-320 ◽  
Author(s):  
Jun-Ming Hong ◽  
Jie-Shan Jiang ◽  
Chang-Tang Chang ◽  
Bor-Yann Chen

1994 ◽  
Vol 61 (4) ◽  
pp. 537-544 ◽  
Author(s):  
Flavia M. L. Passos ◽  
Todd R. Klaenhammer ◽  
Harold E. Swaisgood

SummaryA laboratory scale bioreactor was used for continuous acidification and inoculation of milk with a proteinase-negative, lactose-fermenting strain,Lactococcus lactissubsp.lactisC2S. Calcium alginate-entrapped cells were immobilized on a spiral stainless steel mesh incorporated into a column bioreactor and used to acidify and inoculate reconstituted skim milk. Characteristics of the immobilized cell bioreactor (ICB) were compared with those of a free cell bioreactor (FCB) during challenge with a virulent phage. Steady state biomass and lactate productivities were respectively 25-fold and 12-fold larger with the ICB than with the FCB. The ICB and the FCB were inoculated with the prolate phage c2 at multiplicities of infection of 0·25 and 0·02 respectively. Within 90 min of the infection, the FCB viable cell concentration dropped by five orders of magnitude and never recovered, while the plaque forming units/ml increased dramatically. In the ICB, released cells decreased immediately after infection, but subsequently increased, while the plaque forming units/ml steadily declined, indicating that phage were being washed out of the bioreactor. Productivity of FCB decreased to zero, whereas productivity of the ICB only decreased ∼ 60% and subsequently recovered to its initial steady state value.


2006 ◽  
Vol 53 (11) ◽  
pp. 117-125 ◽  
Author(s):  
E. Tamer ◽  
M.A. Amin ◽  
E.T. Ossama ◽  
M. Bo ◽  
G. Benoit

An algal-bacterial consortium was tested for the treatment from a coke factory. A Chlorella vulgaris strain and a phenol-degrading Alcaligenes sp. were first isolated from the wastewater treatment plant to serve as inocula in the subsequent biodegradation tests. Batch tests were then conducted with samples from the real wastewater or using a synthetic wastewater containing 325 mg phenol/l and 500 mg NH4+/l as target pollutants. Direct biological treatment of the real wastewater was not possible due to the toxicity of organic compounds. Activated carbon adsorption and UV(A-B)-irradiation were efficient in detoxifying the effluent for subsequent biological treatment as inoculation of pretreated samples with the algal-bacterial consortium was followed by complete phenol removal and NH4+ removal of 45%. Complete phenol removal and 33% NH4+ removal were achieved during the fed-batch treatment of artificial wastewater at 6 d hydraulic retention time (HRT). Under continuous feeding at 3.6 d HRT, phenol and NH4+ removal dropped to 58 and 18%, respectively. However, complete phenol removal and 29% NH4+ removal were achieved when 8 g NaHCO3/l was added to the artificial wastewater to enhance algal growth. This study confirms the potential of solar-based industrial wastewater treatment based on solar-based UV pretreatment followed by algal-bacterial biodegradation.


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