Recycling of municipal solid waste incineration fly ash for ordinary Portland cement production: A real-scale test

Abstract The study present in this paper investigates the feasibility of clinker production using water washed MSWI (municipal solid waste incineration) fly ash in addition to cement raw materials. The tested fly ashes were washed and reused as raw material (with dosage of 1% of cement raw material (w/w)). The optimization of the MSWI fly ash washing process was carried out to maximum the extraction of chloride and sulphate. Taking into account economic parameters such as the consumption of water, reaction time and easy operation, the best relation found was a liquid/solid ratio (L/S) of 10/1 during 1/6 h. Pure CO 2 , used to simulate the cement kiln dust gas, was bubbled into the water effluent to decrease the pH by the formation of CaCO 3 . In these conditions, the concentration of heavy metals will decrease as a consequence of the co-precipitation with CaCO 3 . XRD technique was used to monitor the phase formation during the burning of the mixture of MSWI fly ash and cement raw materials. The amounts of trace elements volatilized during clinkerization, as well as leaching behaviours of the clinkers, were also evaluated. After the lab-scale experiments to confirm the efficacy of this technology, a real-scale test (3000 tonnes/day) was conducted. The quality of the resulting cement is sufficient to enable the cement to be put to practical use.

[1]  A Polettini,et al.  Optimization of the solidification/stabilization process of MSW fly ash in cementitious matrices. , 1999, Journal of hazardous materials.

[2]  Toshinori Kojima,et al.  Production of cement clinkers from municipal solid waste incineration (MSWI) fly ash. , 2007, Waste management.

[3]  Ryunosuke Kikuchi,et al.  Recycling of municipal solid waste for cement production: pilot-scale test for transforming incineration ash of solid waste into cement clinker , 2001 .

[4]  Ole Hjelmar,et al.  Disposal strategies for municipal solid waste incineration residues , 1996 .

[5]  J. M. Chimenos,et al.  Optimizing the APC residue washing process to minimize the release of chloride and heavy metals. , 2005, Waste management.

[6]  Jong Heo,et al.  Vitrification of fly ash from municipal solid waste incinerator. , 2002, Journal of hazardous materials.

[7]  P. Shih,et al.  Replacement of raw mix in cement production by municipal solid waste incineration ash , 2003 .

[8]  T. Mangialardi Sintering of MSW fly ash for reuse as a concrete aggregate. , 2001, Journal of hazardous materials.

[9]  M. Hupa,et al.  Absorption of HCl by limestone in hot flue gases. Part II: importance of calcium hydroxychloride , 2005 .

[10]  Tadashi Ito Vitrification of fly ash by swirling-flow furnace , 1996 .

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

[12]  A. K. Suryavanshi,et al.  The binding of chloride ions by sulphate resistant portland cement , 1995 .

[13]  Ferenc D. Tamás,et al.  Chloride ion binding capacity of aluminoferrites , 2001 .

[14]  Zareen Abbas,et al.  Release of salts from municipal solid waste combustion residues. , 2003, Waste management.

[15]  J. Rimstidt,et al.  Interaction of municipal solid waste ash with water. , 1994, Environmental science & technology.

[16]  Chiaki Izumikawa,et al.  Metal recovery from fly ash generated from vitrification process for MSW ash , 1996 .