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Biostabilization assessment of MSW co-disposed with MSWI fly ash in anaerobic bioreactors

Biostabilization assessment of MSW co-disposed with MSWI fly ash in anaerobic bioreactors
Biostabilization assessment of MSW co-disposed with MSWI fly ash in anaerobic bioreactors
Municipal solid waste incinerator (MSWI) fly ash has been examined for possible use as landfill interim cover. For this aim, three anaerobic bioreactors, 1.2 m high and 0.2 m in diameter, were used to assess the co-digestion or co-disposal performance of MSW and MSWI fly ash. Two bioreactors contained ratios of 10 and 20 g fly ash per liter of MSW (or 0.2 and 0.4 g g?1 VS, that is, 0.2 and 0.4 g fly ash per gram volatile solids (VS) of MSW). The remaining bioreactor was used as control, without fly ash addition. The results showed that gas production rate was enhanced by the appropriate addition of MSWI fly ash, with a rate of 6.5 l day?1 kg?1 VS at peak production in the ash-added bioreactors, compared to 4 l day?1 kg?1 VS in control. Conductivity, alkali metals and VS in leachate were higher in the fly ash-added bioreactors compared to control. The results show that MSW decomposition was maintained throughout at near-neutral pH and might be improved by release of alkali and trace metals from fly ash. Heavy metals exerted no inhibitory effect on MSW digestion in all three bioreactors. These phenomena indicate that proper amounts of MSWI fly ash, co-disposed or co-digested with MSW, could facilitate bacterial activity, digestion efficiency and gas production rates
msw, mswi fly ash, anaerobic digestion, landfill, gas production
0304-3894
1233-1242
Lo, H.M.
cf9742e5-ec54-49ed-908d-4ef7ed863e4d
Liu, M.H.
87a3ac27-7b15-478c-be9f-5257168f048c
Pai, T.Y.
7c339e6e-8774-406e-a19c-6aa95fe28988
Lin, C.Y.
6add876f-fe12-44d0-8d55-46c9647efc83
Wang, S.C.
c0a2c8c1-2c1c-4820-91ab-81fc864d3d5d
Banks, C.J.
5c6c8c4b-5b25-4e37-9058-50fa8d2e926f
Hung, C.H.
aee09c65-4c04-4175-ac9f-a67b7f123a9f
Chiang, C.F.
77743e22-852a-43aa-be96-c78cc1a9335f
Lin, K.C.
3de46cbc-cd05-4660-bfc0-85169df577ca
Chen, P.H.
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Chen, J.K.
ad3a4f5b-0b0b-4543-b40f-5638615099e1
Chiu, H.Y.
5e07bd25-bfae-479b-afc5-a1ed9db36359
Su, M.H.
87f68f6d-e7f7-4f88-b3a6-b08b9370bf2d
Kurniawan, T.A.
8a62a316-e8cd-4ea9-acd8-9c39e90837a7
Wu, K.C.
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Hsieh, C.Y.
42623e86-7743-4a26-9e0f-df1014b866fe
Hsu, H.S.
0e7cf238-c45d-43f7-bf0a-e3d9058d115f
Lo, H.M.
cf9742e5-ec54-49ed-908d-4ef7ed863e4d
Liu, M.H.
87a3ac27-7b15-478c-be9f-5257168f048c
Pai, T.Y.
7c339e6e-8774-406e-a19c-6aa95fe28988
Lin, C.Y.
6add876f-fe12-44d0-8d55-46c9647efc83
Wang, S.C.
c0a2c8c1-2c1c-4820-91ab-81fc864d3d5d
Banks, C.J.
5c6c8c4b-5b25-4e37-9058-50fa8d2e926f
Hung, C.H.
aee09c65-4c04-4175-ac9f-a67b7f123a9f
Chiang, C.F.
77743e22-852a-43aa-be96-c78cc1a9335f
Lin, K.C.
3de46cbc-cd05-4660-bfc0-85169df577ca
Chen, P.H.
f41783d9-a578-45af-9a42-4073d6ba9c44
Chen, J.K.
ad3a4f5b-0b0b-4543-b40f-5638615099e1
Chiu, H.Y.
5e07bd25-bfae-479b-afc5-a1ed9db36359
Su, M.H.
87f68f6d-e7f7-4f88-b3a6-b08b9370bf2d
Kurniawan, T.A.
8a62a316-e8cd-4ea9-acd8-9c39e90837a7
Wu, K.C.
086821da-e9c5-4def-9928-f085fd6b7c8c
Hsieh, C.Y.
42623e86-7743-4a26-9e0f-df1014b866fe
Hsu, H.S.
0e7cf238-c45d-43f7-bf0a-e3d9058d115f

Lo, H.M., Liu, M.H., Pai, T.Y., Lin, C.Y., Wang, S.C., Banks, C.J., Hung, C.H., Chiang, C.F., Lin, K.C., Chen, P.H., Chen, J.K., Chiu, H.Y., Su, M.H., Kurniawan, T.A., Wu, K.C., Hsieh, C.Y. and Hsu, H.S. (2009) Biostabilization assessment of MSW co-disposed with MSWI fly ash in anaerobic bioreactors. Journal of Hazardous Materials, 162 (2-3), 1233-1242. (doi:10.1016/j.jhazmat.2008.06.028).

Record type: Article

Abstract

Municipal solid waste incinerator (MSWI) fly ash has been examined for possible use as landfill interim cover. For this aim, three anaerobic bioreactors, 1.2 m high and 0.2 m in diameter, were used to assess the co-digestion or co-disposal performance of MSW and MSWI fly ash. Two bioreactors contained ratios of 10 and 20 g fly ash per liter of MSW (or 0.2 and 0.4 g g?1 VS, that is, 0.2 and 0.4 g fly ash per gram volatile solids (VS) of MSW). The remaining bioreactor was used as control, without fly ash addition. The results showed that gas production rate was enhanced by the appropriate addition of MSWI fly ash, with a rate of 6.5 l day?1 kg?1 VS at peak production in the ash-added bioreactors, compared to 4 l day?1 kg?1 VS in control. Conductivity, alkali metals and VS in leachate were higher in the fly ash-added bioreactors compared to control. The results show that MSW decomposition was maintained throughout at near-neutral pH and might be improved by release of alkali and trace metals from fly ash. Heavy metals exerted no inhibitory effect on MSW digestion in all three bioreactors. These phenomena indicate that proper amounts of MSWI fly ash, co-disposed or co-digested with MSW, could facilitate bacterial activity, digestion efficiency and gas production rates

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More information

Published date: 15 March 2009
Keywords: msw, mswi fly ash, anaerobic digestion, landfill, gas production
Organisations: Civil Engineering & the Environment

Identifiers

Local EPrints ID: 73950
URI: http://eprints.soton.ac.uk/id/eprint/73950
ISSN: 0304-3894
PURE UUID: cc501051-59af-405c-8aa1-b276ceaf6263
ORCID for C.J. Banks: ORCID iD orcid.org/0000-0001-6795-814X

Catalogue record

Date deposited: 11 Mar 2010
Last modified: 14 Mar 2024 02:39

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Contributors

Author: H.M. Lo
Author: M.H. Liu
Author: T.Y. Pai
Author: C.Y. Lin
Author: S.C. Wang
Author: C.J. Banks ORCID iD
Author: C.H. Hung
Author: C.F. Chiang
Author: K.C. Lin
Author: P.H. Chen
Author: J.K. Chen
Author: H.Y. Chiu
Author: M.H. Su
Author: T.A. Kurniawan
Author: K.C. Wu
Author: C.Y. Hsieh
Author: H.S. Hsu

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