Treatment of Resorcinol and Phenol Bearing Waste Water by Simultaneous Adsorption Biodegradation (SAB): Optimization of Process Parameters

In the present paper the observations on the simultaneous adsorption biodegradation (SAB) of resorcinol and phenol from two separate synthetic wastewater samples have been reported. For SAB, immobilization of Pseudomonas putida MTCC 1194 on granular activated carbon (GAC) has been done. The optimum process parameters like adsorbent dose, particle size of GAC, and pH have been determined experimentally by calculating percentage removal. The optimum process parameters have also been verified by the theoretical model of Weber and Morris (1963). Under the experimental conditions at 28 degrees Celsius the optimum process parameters are noted as adsorbent dose = 10 g/l, GAC particle size = 2- 4 mm and pH = 6.24. The isotherm studies of these processes have been done. Adsorption studies have also been done separately for both the compounds for comparing the efficiency of SAB over adsorption.

[1]  G. Mckay,et al.  Adsorption of pollutants on to activated carbon in fixed beds , 2007 .

[2]  B. Mohanty,et al.  Laboratory based approaches for arsenic remediation from contaminated water: recent developments. , 2006, Journal of hazardous materials.

[3]  B. Özkaya Adsorption and desorption of phenol on activated carbon and a comparison of isotherm models. , 2006 .

[4]  I. D. Mall,et al.  Adsorptive removal of phenol by bagasse fly ash and activated carbon: Equilibrium, kinetics and thermodynamics , 2006 .

[5]  A. Telefoncu,et al.  Biodegradation of phenol by Pseudomonas putida immobilized on activated pumice particles , 2005 .

[6]  M. Zilli,et al.  Mathematical modelling and simulation of phenol degradation in biofilters , 2004 .

[7]  T. Bley,et al.  Rapid monitoring of the biodegradation of phenol-like compounds by the yeast Candida maltosa using BOD measurements , 2004 .

[8]  E. Bayraktar,et al.  Kinetics model for growth of Pseudomonas putida F1 during benzene, toluene and phenol biodegradation , 2004 .

[9]  R. Juang,et al.  Mass transfer effect and intermediate detection for phenol degradation in immobilized Pseudomonas putida systems , 2003 .

[10]  G. González,et al.  Biodegradation of phenolic industrial wastewater in a fluidized bed bioreactor with immobilized cells of Pseudomonas putida. , 2001, Bioresource technology.

[11]  D. Das,et al.  Reaction engineering studies on biodegradation of phenol by Pseudomonas putida MTCC 1194 immobilized on calcium alginate , 2001 .

[12]  J. Modak,et al.  Mathematical model for evaluation of mass transfer limitations in phenol biodegradation by immobilized Pseudomonas putida. , 2001, Journal of biotechnology.

[13]  G Thompson,et al.  The treatment of pulp and paper mill effluent: a review. , 2001, Bioresource technology.

[14]  Rodrigues,et al.  Phenol biodegradation by Pseudomonas putida DSM 548 in a batch reactor. , 2000, Biochemical engineering journal.

[15]  G. Annadurai,et al.  Adsorption and bio-degradation of phenol by chitosan-immobilized Pseudomonas putida (NICM 2174) , 2000 .

[16]  C. Kuek,et al.  Continuous degradation of phenol at low concentration using immobilized Pseudomonas putida , 1999 .

[17]  K. Loh,et al.  Modeling the role of metabolic intermediates in kinetics of phenol biodegradation , 1999 .

[18]  Chi Tien,et al.  Bacterial film growth in adsorbent surfaces , 1981 .

[19]  Surendra Kumar,et al.  Biodegradation kinetics of phenol and catechol using Pseudomonas putida MTCC 1194 , 2005 .

[20]  H. Ngo,et al.  Biofilter in water and wastewater treatment , 2003 .

[21]  P. Kumaran,et al.  Kinetics of phenol biotransformation , 1997 .

[22]  R. Méndez,et al.  Biofilm Reactors Technology in Wastewater Treatment , 1992 .

[23]  G. Mckay,et al.  The adsorption of various pollutants from aqueous solutions on to activated carbon , 1985 .

[24]  D. Bhatt,et al.  Effect of pH on phenol removal in moving media reactors , 1983 .

[25]  W. Weber,et al.  Kinetics of Adsorption on Carbon from Solution , 1963 .