Pilot-scale study of phosphorus recovery through struvite crystallization examining the process feasibility

The suitability of a new pilot-scale reactor to recover phosphorus through struvite crystallization was examined. Based on the similar principles previously tested in bench-scale reactors and scaled up to overcome operating problems encountered in earlier work, the pilot-scale crystallizer was used to effectively remove–recover phosphorus from synthetic wastewaters. Ortho-P removal rates as high as 90% were obtained for low (~50–70 mg/L P) and medium (~70–100 mg/L P) strength wastewaters. To achieve these removal rates, a relatively high pH value of 8.3 was required. Over 90% of the removed phosphates could be recovered in the form of harvestable struvite crystals with a mean size of 2.5–3.5 mm and sufficient mechanical strength to permit harvesting–reuse. A new concept of crystal retention time (CRT) has been developed, which is used to make estimates of the struvite crystal age. Results of this study indicate that CRT is one of the main factors affecting the mean crystal size.Key words: crystallization,...

[1]  D. Mavinic,et al.  Preliminary investigation into factors affecting controlled struvite crystallization at the bench scale , 2004 .

[2]  A. Adnan Pilot-scale study of phosphorus recovery through struvite crystallization , 2003 .

[3]  S. Parsons,et al.  Struvite formation, control and recovery. , 2002, Water research.

[4]  P Pearce,et al.  Potential phosphorus recovery by struvite formation. , 2002, Water research.

[5]  J. Lester,et al.  Conditions influencing the precipitation of magnesium ammonium phosphate. , 2001, Water research.

[6]  Y Ueno,et al.  Three Years Experience of Operating and Selling Recovered Struvite from Full-Scale Plant , 2001, Environmental technology.

[7]  I. Celen,et al.  Recovery of Ammonia as Struvite from Anaerobic Digester Effluents , 2001, Environmental technology.

[8]  F Cecchi,et al.  Phosphorus removal from a real anaerobic supernatant by struvite crystallization. , 2001, Water research.

[9]  M. Loizidou,et al.  Pretreatment of natural clinoptilolite in a laboratory-scale ion exchange packed bed. , 2001, Water research.

[10]  Mahazareen Behram Dastur Investigation into the factors affecting controlled struvite crystallization at the bench-scale , 2001 .

[11]  E. V. Münch,et al.  Controlled struvite crystallisation for removing phosphorus from anaerobic digester sidestreams. , 2001, Water research.

[12]  Glen T. Daigger,et al.  Phosphorus Recovery Technology Modeling and Feasibility Evaluation for Municipal Wastewater Treatment Plants , 1999 .

[13]  I. Steen,et al.  Why Recover Phosphorus for Recycling, and How? , 1999 .

[14]  P. Hobbs,et al.  Prospects for the Recovery of Phosphorus from Animal Manures: A Review , 1999 .

[15]  D. Mavinic,et al.  Anaerobic Co-Digestion of Combined Sludges from a Bnr Wastewater Treatment Plant , 1998 .

[16]  H. Pöpel,et al.  Behavior of waste activated sludge from enhanced biological phosphorus removal during sludge treatment , 1996 .

[17]  Marcelo Martins Seckler,et al.  Phosphate removal in a fluidized bed—II. Process optimization , 1996 .

[18]  D. Niedbala Pilot-scale studies of the anaerobic digestion of combined wastewater sludges and mitigation of phosphorus release , 1995 .

[19]  D. Jenkins,et al.  Determination of ferric chloride dose to control struvite precipitation in anaerobic sludge digesters , 1994 .

[20]  D. Toerien,et al.  Fish production in small oxidation ponds , 1988 .

[21]  J. Borgerding Phosphate deposits in digestion systems , 1972 .