Model-based design of different fedbatch strategies for phenol degradation in acclimatized activated sludge cultures

2011 ◽  
Vol 102 (4) ◽  
pp. 3740-3747 ◽  
Author(s):  
Chérif Ben-Youssef ◽  
Gabriela A. Vázquez-Rodríguez
Keyword(s):  
Activated Sludge ◽  
Phenol Degradation ◽  
Model Based

Modelling of activated sludge for textile wastewaters

1998 ◽  
Vol 38 (4-5) ◽  
pp. 9-17 ◽  
Author(s):  
F. Germirli Babuna ◽  
D. Orhon ◽  
E. Ubay Çokgör ◽  
G. Insel ◽  
B. Yaprakli
Keyword(s):  
Activated Sludge ◽  
Comprehensive Evaluation ◽  
Component Model ◽  
Activated Sludge Process ◽  
Experimental Basis ◽  
Model Simulations ◽  
Effluent Quality ◽  
Model Based ◽  
Major Process ◽  
Textile Wastewaters

A comprehensive evaluation of four different textile wastewaters was carried out to set the experimental basis for the modelling of activated sludge process. Experiments involved beside conventional characterization, detailed COD fractionation and assessment of major kinetic and stoichiometric coefficients by means of respirometric measurements. A multi-component model based on the endogenous decay concept was used for the kinetic interpretation and design of activated sludge. The fate and variation of major process components affecting effluent quality with the sludge age were evaluated by means of model simulations.

Optimizing the Step-Feed Ratio and Modeling the Effluents of Aerobic Tank with ASM1 in ECOSUNIDE Process

2012 ◽  
Vol 178-181 ◽  
pp. 526-530
Author(s):  
Ruo Gu Li ◽  
Yan Qiu Zhang
Keyword(s):  
Organic Matter ◽  
Activated Sludge ◽  
Ammonia Nitrogen ◽  
Feed Ratio ◽  
Optimum Ratio ◽  
Matlab Simulink ◽  
Activated Sludge Model ◽  
Model Based ◽  
Autotrophic Bacteria ◽  
Optimum Model

The step feed model based on the Activated Sludge Model No.1 (ASM1) and the optimum model of the ammonia nitrogen (SNH) removal in wastewater were established. Four aeration tanks under the different step feed ratios were simulated by Matlab Simulink. The results show that single-feeding is conducive to the removal of readily biodegradable substrate (SS) and the growth of heterotrophic organisms (XBH), and to lower the biodegradable substrate (XS) at the same time. The SS, XS, and SNH concentrations are 1.36, 5.98, and 3.02 mg/L respectively in effluent. However, the step-feeding is conducive to the SNH removal, and the autotrophic bacteria (XBA) growth. Under the step feed ratio (25/25/25/25%), the SS, XS, and SNH concentrations are 2.64, 10.79, and 2.61 mg/L respectively. Under the optimum ratio (28.7/23.6/20.4/27.2%), step-feeding could further facilitate the removal of SNH and hinder the removal of organic matter, their concentrations are 2.70, 10.98, and 2.47 mg/L respectively.

scholarly journals Environmental biological model based on optimization of activated sludge process

2008 ◽  
Vol 6 (1) ◽  
pp. 69-76 ◽  
Author(s):  
X. X. Zhang ◽  
D. Y. Zhao ◽  
Z. X. Wang ◽  
B. Wu ◽  
W. X. Li ◽  
...  
Keyword(s):  
Activated Sludge ◽  
Biological Model ◽  
Activated Sludge Process ◽  
Model Based

Characteristics of phenol degradation in saline conditions of a halophilic strain JS3 isolated from industrial activated sludge

2015 ◽  
Vol 99 (1-2) ◽  
pp. 230-234 ◽  
Author(s):  
Yu Jiang ◽  
Kai Yang ◽  
Hongyu Wang ◽  
Yu Shang ◽  
Xiaojun Yang
Keyword(s):  
Activated Sludge ◽  
Phenol Degradation

Fuzzy model-based predictive control of dissolved oxygen in activated sludge processes

2014 ◽  
Vol 136 ◽  
pp. 88-95 ◽  
Author(s):  
Ting Yang ◽  
Wei Qiu ◽  
You Ma ◽  
Mohammed Chadli ◽  
Lixian Zhang
Keyword(s):  
Dissolved Oxygen ◽  
Activated Sludge ◽  
Predictive Control ◽  
Fuzzy Model ◽  
Model Based ◽  
Activated Sludge Processes

Biodegradation of High Phenol Concentration in a Membrane Bioreactor

2008 ◽  
Vol 6 (1) ◽  
Author(s):  
Benoît Marrot ◽  
Adrian Barrios-Martinez ◽  
Philippe Moulin ◽  
Nicolas Roche
Keyword(s):  
Activated Sludge ◽  
Removal Efficiency ◽  
Membrane Bioreactor ◽  
Substrate Inhibition ◽  
Phenol Degradation ◽  
Phenol Concentration ◽  
Phenol Removal ◽  
Permeate Flux ◽  
Phenol Biodegradation ◽  
Haldane Model

Phenol biodegradation by mixed culture was studied in a membrane bioreactor (MBR) over a period of 285 days. Activated sludge was used as the MBR biomass, after controlled acclimation to high phenol concentrations. The MBR permeate flux was stabilized quickly (in a few hours) and always maintained above 90 L.h-1.m-2.bar-1. The acclimatized activated sludge allowed significant phenol degradation (95% average COD removal efficiency and greater than 99% phenol removal efficiency) without supplemental reagent addition. After sludge acclimatization, the Haldane kinetics model for a single substrate was used to obtain the maximum specific growth rate (µm = 0.438 h-1), the half saturation coefficient (Ks = 29.54 mg.L-1) and the substrate inhibition constant (Ki = 72.45 mg.L-1). Biodegradation experiments were conducted at different phenol concentrations (4.9 – 8.5 g.L-1 d-1). Although the phenol concentration was high, the Haldane model was still acceptable, and removal capacities were in agreement with literature. Excellent effluent quality was obtained regardless of the extremely short SRT (5 – 17 days). This work shows the potential of MBR for toxic chemical elimination, charged effluents treatment and process stability.

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