Evaluation of pre-treatment methods for landfill disposal of residues from municipal solid waste incineration

This study presents results concerning leaching of Pb, Cd, Ca, and Cl with reference to one individual batch of bottom ash and fly ash (5:1) resulting from a municipal solid waste incinerator (MSWI) in Japan. This ash mixture was stabilised by the following pre-treatments: water washing, carbonation, and phosphate stabilisation. Once the optimum processing condition for each pre-treatment was determined, the performances were evaluated using both pH-stat leaching (pH 6, 9, 12) and availability tests. These performance tests were carried out with only fly ash without considering the mixture of MSWI residues, in order to accurately determine leaching differences among the pre-treatments. Water washing effectively removed the major elements from MSWI residues and also reduced the leachability of trace metals, such as Pb and Cd. A washing time of 15 minutes with a liquid/solid ratio of 5 was reasonably effective. Carbonation had a significant effect on leachability in alkaline ranges (pH 9 and 12), when the reaction occurred only on the surface of MSWI residues, moreover a moisture content of 10-16.7% was proved suitable for carbonation. On the other hand, phosphate stabilisation, even with small amounts of phosphate (0.16 mol-PO4 3- kg-1), was very effective in reducing the leach-ability of heavy metals.

[1]  S. Cernuschi,et al.  Leaching of Residues From Msw Incineration , 1990 .

[2]  J. E. Krzanowski,et al.  Heavy metal stabilization in municipal solid waste combustion bottom ash using soluble phosphate , 2000 .

[3]  Kuen-Sheng Wang,et al.  Effects of a water-extraction process on heavy metal behavior in municipal solid waste incinerator fly ash , 2001 .

[4]  Holger Ecke,et al.  Carbonation for Fixation of Metals in Municipal Solid Waste Incineration (MSWI) Fly Ash , 2001 .

[5]  Brian W. Baetz,et al.  Lysimeter Washing of Msw Incinerator Bottom Ash , 1995 .

[6]  Peter Baccini,et al.  Chemical behaviour of municipal solid waste incinerator bottom ash in monofills , 1992 .

[7]  Alessandra Polettini,et al.  Acid neutralisation capacity and hydration behaviour of incineration bottom ash–Portland cement mixtures , 2002 .

[8]  K. J. Reddy,et al.  Reaction of CO2 with alkaline solid wastes to reduce contaminant mobility , 1994 .

[9]  T. Taylor Eighmy,et al.  Heavy Metal Stabilization in Municipal Solid Waste Combustion Dry Scrubber Residue Using Soluble Phosphate , 1997 .

[10]  Gerhard Furrer,et al.  Influence of biodegradation processes on the duration of CaCO3 as a pH buffer in municipal solid waste incinerator bottom ash. , 2002, Environmental science & technology.

[11]  Kohei Urano,et al.  An Estimation Method for CO2 Emission from Municipal Waste Incinerators by Continuous O2 Analyzer , 2001 .

[12]  Shin-ichi Sakai,et al.  Municipal solid waste management in Japan , 1996 .

[13]  Boonyong Lohwongwatana,et al.  Industrial hazardous waste treatment facilities in Thailand , 1990 .

[14]  Seiichi Abe,et al.  Leaching Behavior of Untreated and Phosphate Treated Fly Ash from Municipal Solid Waste Melting Facilities and Minerals Formed in Phosphate Treated Fly Ash , 1999 .