Anaerobic treatment of high-strength cheese-whey wastewaters in laboratory and pilot UASB-reactors

Abstract Start-up of the laboratory (3 l) UASB-reactor treating raw high-strength (up to 77 g COD/l) cheese-whey wastewaters as well as the treatment efficiencies (TE) and the maximal admissible organic loading rates (OLR) have been investigated under mesophilic (35°C) and submesophilic (20–30°C) conditions. A stable operation of the reactor with the TE higher than 90% on the total COD has been demonstrated up to the OLR of 28.5 and 9.5 g COD/l·day for mesophilic and submesophilic regimes, respectively. A successful start-up of the pilot (10.74 m 3 ) non-thermostated UASB-reactor treating raw cheese-whey wastewaters at ambient temperatures (ca. 24°C) has been completed in 3 months. Further exploitation of the reactor at the design OLR of 6.5 g COD/l·day showed its good operational stability with the TE close to 95% on the basis of total COD. After a proper start-up, the UASB-reactors can cope with preacidificated cheese-whey wastewaters (pH of about 4) even at elevated OLR that eliminates the necessity of alkalinity supplementation.

[1]  Michael S. Switzenbaum,et al.  Anaerobic expanded bed treatment of whey , 1982 .

[2]  I. Callander,et al.  Anaerobic digestion of high‐strength cheese whey utilizing semicontinuous digesters and chemical flocculant addition , 1986, Biotechnology and bioengineering.

[3]  A. E. Greenberg,et al.  Standard methods for the examination of water and wastewater : supplement to the sixteenth edition , 1988 .

[4]  T. J. Britz,et al.  Anaerobic digestion of deproteinated cheese whey , 1985, Journal of Dairy Research.

[5]  A. Tilche,et al.  Cheese whey and cheese factory wastewater treatment with a biological anaerobic-aerobic process , 1995 .

[6]  Paul H. Boening,et al.  Anaerobic fluidized bed whey treatment , 1982, Biotechnology and bioengineering.

[7]  Michael S. Switzenbaum,et al.  Anaerobic treatment: Temperature and nutrient effects , 1984 .

[8]  Santosh N. Kaul,et al.  Determination of kinetic constants for a two-stage anaerobic upflow packed-bed reactor for dairy wastewater. , 1992 .

[9]  A. J. Mawson,et al.  Bioconversions for whey utilization and waste abatement , 1994 .

[10]  S. Varfolomeyev,et al.  Kinetic regularities of methane production by a methanogenic association , 1989 .

[11]  María Carmen Veiga,et al.  Start-Up, Operation, Monitoring and Control of High-Rate Anaerobic Treatment Systems , 1991 .

[12]  Kwang Victor Lo,et al.  Digestion of cheese whey with anaerobic rotating biological contact reactors , 1986 .

[13]  I. Dunn,et al.  Packed‐ and fluidized‐bed biofilm reactor performance for anaerobic wastewater treatment , 1988, Biotechnology and bioengineering.

[14]  Emilige W. Schröder,et al.  Anaerobic digestion of deproteinated cheese whey in an Upflow Sludge Blanket reactor , 1989, Journal of Dairy Research.

[15]  J. N. Clark Utilization of acid and sweet wheys in a pilot-scale upflow anaerobic sludge blanket digester. , 1988 .

[16]  Sergey Kalyuzhnyi,et al.  Organic removal and microbiological features of UASB-reactor under various organic loading rates , 1996 .

[17]  K L Pinder,et al.  Instability caused by high strength of cheese whey in a UASB reactor , 1993, Biotechnology and bioengineering.

[18]  Pilot-scale anaerobic treatment of cheese whey by the substrate shuttle process , 1994 .

[19]  K. V. Lo,et al.  Anaerobic digestion of cheese whey using up-flow anaerobic sludge blanket reactor , 1989 .