Detoxification of ashes from a fluidized bed waste incinerator
•Bottom and fly ashes were subject to TCLP test.•Leachates of finer bottom ash and fly ash may exceed the regulatory limit.•Thermal treatment of fly ash for removal of heavy metals were carried out.•Almost all Cd, Pb and more than 90% of Cu and 95% of Zn could be removed.•A maximum 20% of Cr was rem...
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Published in | Chemosphere (Oxford) Vol. 134; pp. 346 - 354 |
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Main Authors | , , , , , |
Format | Journal Article |
Language | English |
Published |
England
Elsevier Ltd
01.09.2015
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Abstract | •Bottom and fly ashes were subject to TCLP test.•Leachates of finer bottom ash and fly ash may exceed the regulatory limit.•Thermal treatment of fly ash for removal of heavy metals were carried out.•Almost all Cd, Pb and more than 90% of Cu and 95% of Zn could be removed.•A maximum 20% of Cr was removed due to formation of stable Cr compounds.
This paper was to test and control the toxicity of bottom and fly ashes from a circulated fluidized bed (CFB) incinerator. Bottom and fly ashes were firstly subject to TCLP test. Even though leachates of most particle size of bottom ash were below regulatory limit, the leachates of finer bottom ash may exceed the regulatory limit. Therefore, finer bottom ash should be separated and treated before landfilled directly or used as cement replacement. Due to high amounts of leached heavy metals, thermal treatment of fly ash was carried out to remove heavy metals. The influence of temperature, residence time, metal chloride and gas velocity were studied. In all conditions, Cd can be well removed. Pb can be almost completely removed with MgCl2 addition at 1000°C in 1h. The removal of Zn and Cu was accelerated significantly by MgCl2 and higher temperature separately. At optimum conditions, more than 90% of Cu and 95% of Zn could be removed, while a maximum 20% of Cr was removed due to the existence or formation of CaCr2O4, MgCr2O4 and K2Cr2O4 in raw or treated fly ashes. |
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AbstractList | This paper was to test and control the toxicity of bottom and fly ashes from a circulated fluidized bed (CFB) incinerator. Bottom and fly ashes were firstly subject to TCLP test. Even though leachates of most particle size of bottom ash were below regulatory limit, the leachates of finer bottom ash may exceed the regulatory limit. Therefore, finer bottom ash should be separated and treated before landfilled directly or used as cement replacement. Due to high amounts of leached heavy metals, thermal treatment of fly ash was carried out to remove heavy metals. The influence of temperature, residence time, metal chloride and gas velocity were studied. In all conditions, Cd can be well removed. Pb can be almost completely removed with MgCl2 addition at 1000 degree C in 1h. The removal of Zn and Cu was accelerated significantly by MgCl2 and higher temperature separately. At optimum conditions, more than 90% of Cu and 95% of Zn could be removed, while a maximum 20% of Cr was removed due to the existence or formation of CaCr2O4, MgCr2O4 and K2Cr2O4 in raw or treated fly ashes. This paper was to test and control the toxicity of bottom and fly ashes from a circulated fluidized bed (CFB) incinerator. Bottom and fly ashes were firstly subject to TCLP test. Even though leachates of most particle size of bottom ash were below regulatory limit, the leachates of finer bottom ash may exceed the regulatory limit. Therefore, finer bottom ash should be separated and treated before landfilled directly or used as cement replacement. Due to high amounts of leached heavy metals, thermal treatment of fly ash was carried out to remove heavy metals. The influence of temperature, residence time, metal chloride and gas velocity were studied. In all conditions, Cd can be well removed. Pb can be almost completely removed with MgCl2 addition at 1000°C in 1h. The removal of Zn and Cu was accelerated significantly by MgCl2 and higher temperature separately. At optimum conditions, more than 90% of Cu and 95% of Zn could be removed, while a maximum 20% of Cr was removed due to the existence or formation of CaCr2O4, MgCr2O4 and K2Cr2O4 in raw or treated fly ashes. This paper was to test and control the toxicity of bottom and fly ashes from a circulated fluidized bed (CFB) incinerator. Bottom and fly ashes were firstly subject to TCLP test. Even though leachates of most particle size of bottom ash were below regulatory limit, the leachates of finer bottom ash may exceed the regulatory limit. Therefore, finer bottom ash should be separated and treated before landfilled directly or used as cement replacement. Due to high amounts of leached heavy metals, thermal treatment of fly ash was carried out to remove heavy metals. The influence of temperature, residence time, metal chloride and gas velocity were studied. In all conditions, Cd can be well removed. Pb can be almost completely removed with MgCl2 addition at 1000°C in 1h. The removal of Zn and Cu was accelerated significantly by MgCl2 and higher temperature separately. At optimum conditions, more than 90% of Cu and 95% of Zn could be removed, while a maximum 20% of Cr was removed due to the existence or formation of CaCr2O4, MgCr2O4 and K2Cr2O4 in raw or treated fly ashes.This paper was to test and control the toxicity of bottom and fly ashes from a circulated fluidized bed (CFB) incinerator. Bottom and fly ashes were firstly subject to TCLP test. Even though leachates of most particle size of bottom ash were below regulatory limit, the leachates of finer bottom ash may exceed the regulatory limit. Therefore, finer bottom ash should be separated and treated before landfilled directly or used as cement replacement. Due to high amounts of leached heavy metals, thermal treatment of fly ash was carried out to remove heavy metals. The influence of temperature, residence time, metal chloride and gas velocity were studied. In all conditions, Cd can be well removed. Pb can be almost completely removed with MgCl2 addition at 1000°C in 1h. The removal of Zn and Cu was accelerated significantly by MgCl2 and higher temperature separately. At optimum conditions, more than 90% of Cu and 95% of Zn could be removed, while a maximum 20% of Cr was removed due to the existence or formation of CaCr2O4, MgCr2O4 and K2Cr2O4 in raw or treated fly ashes. •Bottom and fly ashes were subject to TCLP test.•Leachates of finer bottom ash and fly ash may exceed the regulatory limit.•Thermal treatment of fly ash for removal of heavy metals were carried out.•Almost all Cd, Pb and more than 90% of Cu and 95% of Zn could be removed.•A maximum 20% of Cr was removed due to formation of stable Cr compounds. This paper was to test and control the toxicity of bottom and fly ashes from a circulated fluidized bed (CFB) incinerator. Bottom and fly ashes were firstly subject to TCLP test. Even though leachates of most particle size of bottom ash were below regulatory limit, the leachates of finer bottom ash may exceed the regulatory limit. Therefore, finer bottom ash should be separated and treated before landfilled directly or used as cement replacement. Due to high amounts of leached heavy metals, thermal treatment of fly ash was carried out to remove heavy metals. The influence of temperature, residence time, metal chloride and gas velocity were studied. In all conditions, Cd can be well removed. Pb can be almost completely removed with MgCl2 addition at 1000°C in 1h. The removal of Zn and Cu was accelerated significantly by MgCl2 and higher temperature separately. At optimum conditions, more than 90% of Cu and 95% of Zn could be removed, while a maximum 20% of Cr was removed due to the existence or formation of CaCr2O4, MgCr2O4 and K2Cr2O4 in raw or treated fly ashes. |
Author | Ma, Chuan Sun, Lushi Qiao, Yu Jin, Limei Yu, Jie Wang, Wenxia |
Author_xml | – sequence: 1 givenname: Jie surname: Yu fullname: Yu, Jie – sequence: 2 givenname: Yu surname: Qiao fullname: Qiao, Yu email: yuqiao@mail.hust.edu.cn – sequence: 3 givenname: Lushi surname: Sun fullname: Sun, Lushi email: sunlushi@hust.edu.cn – sequence: 4 givenname: Limei surname: Jin fullname: Jin, Limei – sequence: 5 givenname: Wenxia surname: Wang fullname: Wang, Wenxia – sequence: 6 givenname: Chuan surname: Ma fullname: Ma, Chuan |
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CitedBy_id | crossref_primary_10_1021_acs_energyfuels_9b02187 crossref_primary_10_1016_j_energy_2020_117773 crossref_primary_10_7717_peerj_9693 crossref_primary_10_1016_j_chemosphere_2019_125107 crossref_primary_10_1016_j_wasman_2015_12_015 crossref_primary_10_1007_s12649_018_0476_6 crossref_primary_10_1177_0734242X211003968 |
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Keywords | TCLP Fluidized bed incinerator Municipal solid waste Heavy metal Thermal treatment |
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Snippet | •Bottom and fly ashes were subject to TCLP test.•Leachates of finer bottom ash and fly ash may exceed the regulatory limit.•Thermal treatment of fly ash for... This paper was to test and control the toxicity of bottom and fly ashes from a circulated fluidized bed (CFB) incinerator. Bottom and fly ashes were firstly... |
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SubjectTerms | Ashes bottom ash cadmium cement Chromium Coal Ash Copper Fluidized bed incinerator Fluidized beds Fly ash heat treatment Heavy metal Heavy metals Inactivation, Metabolic Incineration - methods Incinerators Leachates lead magnesium chloride Metals, Heavy - toxicity Municipal solid waste Particle Size TCLP temperature Thermal treatment toxicity zinc |
Title | Detoxification of ashes from a fluidized bed waste incinerator |
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