Characterization of the loosely attached fraction of activated sludge bacteria

2008 ◽  
Vol 42 (4-5) ◽  
pp. 843-854 ◽  
Author(s):  
Fernando Morgan-Sagastume ◽  
Poul Larsen ◽  
Jeppe Lund Nielsen ◽  
Per Halkjær Nielsen
2021 ◽  
Author(s):  
Gang Zhao ◽  
Yanan Wu ◽  
Xu Wang ◽  
Meng Chen ◽  
Li Li

Abstract Plasmid-mediated bioaugmentation has potential application in the cleanup of recalcitrant environmental pollutants. In this study, we examined the influence of various contaminants (in different categories or different amounts) as a selection pressure on the transfer of catabolic plasmids within an activated sludge bacteria community bioaugmented with Rhodococcus sp. strain p52 harboring pDF01 and pDF02. The distinguishable genera of transconjugants were isolated under the stresses of phenanthrene, dibenzothiophene, and dibenzo-p-dioxin. The difference in genomic G + C content (5.0 ~ 27.5%) between transconjugants and strain p52 indicated the transfer of the catabolic plasmids crossing phylogenetic boundaries. The specific removal rates in activated sludge reactors for phenanthrene, dibenzothiophene, and dibenzo-p-dioxin were elevated in turn. The three contaminants exerted different degrees of influence on the activated sludge bacteria bearing the catabolic plasmids. The highest proportion of transconjugants was detected in the reactor fed with dibenzo-p-dioxin. Additionally, as dibenzo-p-dioxin from 10 to 80 mg/L was fed into the reactors, the proportion of transconjugants increased. Film mating tests demonstrated that the plasmid transfer frequency varied among recipients under the contaminant stresses of phenanthrene, dibenzothiophene, and dibenzo-p-dioxin. Our study provides a characterization of the recalcitrant contaminants as a selection pressure that can modulate catabolic plasmid transfer during genetic bioaugmentation for the removal of contaminants.


1998 ◽  
Vol 37 (4-5) ◽  
pp. 95-98 ◽  
Author(s):  
Nancy G. Love ◽  
Mary E. Rust ◽  
Kathy C. Terlesky

An anaerobic enrichment culture was developed from an anoxic/anaerobic/aerobic activated sludge sequencing batch reactor using methyl ethyl ketoxime (MEKO), a potent nitrification inhibitor, as the sole carbon and energy source in the absence of molecular oxygen and nitrate. The enrichment culture was gradually fed decreasing amounts of biogenic organic compounds and increasing concentrations of MEKO over 23 days until the cultures metabolized the oxime as the sole carbon source; the cultures were maintained for an additional 41 days on MEKO alone. Turbidity stabilized at approximately 100 mg/l total suspended solids. Growth on selective media plates confirmed that the microorganisms were utilizing the MEKO as the sole carbon and energy source. The time frame required for growth indicated that the kinetics for MEKO degradation are slow. A batch test indicated that dissolved organic carbon decreased at a rate comparable to MEKO consumption, while sulfate was not consumed. The nature of the electron acceptor in anaerobic MEKO metabolism is unclear, but it is hypothesized that the MEKO is hydrolyzed intracellularly to form methyl ethyl ketone and hydroxylamine which serve as electron donor and electron acceptor, respectively.


2008 ◽  
Vol 20 (5) ◽  
pp. 536-542 ◽  
Author(s):  
Kangala B. Chipasa ◽  
Krystyna Mdrzycka
Keyword(s):  

2007 ◽  
Vol 30 (12) ◽  
pp. 731-736
Author(s):  
Keishi WADA ◽  
Daisuke SANO ◽  
Takahiro IMAI ◽  
Tatsuo OMURA

1992 ◽  
Vol 25 (6) ◽  
pp. 125-139 ◽  
Author(s):  
J. Kappeler ◽  
W. Gujer

To predict the behaviour of biological wastewater treatment plants, the Activated Sludge Model No. 1 is often used. For the application of this model kinetic parameters and wastewater composition must be known. A simple method to estimate kinetic parameters of heterotrophic biomass and COD wastewater fractions is presented. With three different types of batch-tests these parameters and fractions can be determined by measuring oxygen respiration. Our measurements showed that the maximum specific growth rate µmax of heterotrophic biomass depends on temperature, reactor configuration and SRT. In typical wastewater treatment plants of Switzerland the amount of readily biodegradable substrate was generally small (about 9 % of the COD in primary effluent). The same method can also be used to determine kinetic parameters of nitrifying biomass.


Chemosphere ◽  
1999 ◽  
Vol 38 (15) ◽  
pp. 3555-3570 ◽  
Author(s):  
U.J. Strotmann ◽  
A. Geldem ◽  
A. Kuhn ◽  
C. Gendig ◽  
S. Klein

1998 ◽  
Vol 38 (1) ◽  
pp. 303-310 ◽  
Author(s):  
V. Naidoo ◽  
V. Urbain ◽  
C. A. Buckley

Denitrification kinetics and wastewater characterization of eight different plants in Europe are discussed. Denitrification batch tests revealed three distinct rates except in the cases of Plaisir, Rostock and Orense where 4 rates were observed. The latter three plants revealed atypical rapid initial rates which were between 7 and 21 mgN/gVSS.h. All denitrification kinetics under non-limiting carbon conditions revealed fast first rates which ranged between 3.0 and 7.3 mgN/gVSS.h. Acetate was used to simulate denitrification kinetics with readily biodegradable COD present. Two subsequent rates were observed. Rates 2 and 3 ranged between 2 and 3 mgN/gVSS.h, and 1 and 2 mgN/gVSS.h, respectively. The RBCOD fraction varied between 10 and 19%, except for one of the plants where the value determined was 7%.


1992 ◽  
Vol 26 (1-2) ◽  
pp. 377-386 ◽  
Author(s):  
F. Çeçen

Laboratory-scale physicochemical and biological treatability studies were performed on wastewaters discharged from an industry producing household and heavy-duty detergents of powder and liquid type. The characterization of effluents led to the conclusion that the industry was highly pollutant in terms of BOD5, COD, surfactant, phosphorus, oil-grease, suspended solids and pH. By the use of lime in the precipitation stage about 80 % of COD and more than 90 % of phosphorus and anionic surface active agents could be removed. Following the treatment with lime the biodegradation of these wastewaters was investigated in continuously fed activated sludge units. The biokinetic constants of the reaction were determined as k = 0.76 d−1, Ks = 972 mg/l COD, a = 0.58 mg O2/mg COD, b = 0.044 mg O2/mg MLVSS.d. The experimental findings were used in the design of a full-scale treatment system.


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