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 inChemosphere (Oxford) Vol. 134; pp. 346 - 354
Main Authors Yu, Jie, Qiao, Yu, Sun, Lushi, Jin, Limei, Wang, Wenxia, Ma, Chuan
Format Journal Article
LanguageEnglish
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.
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
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Keywords TCLP
Fluidized bed incinerator
Municipal solid waste
Heavy metal
Thermal treatment
Language English
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SSID ssj0001659
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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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StartPage 346
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
URI https://dx.doi.org/10.1016/j.chemosphere.2015.04.045
https://www.ncbi.nlm.nih.gov/pubmed/25973859
https://www.proquest.com/docview/1686414178
https://www.proquest.com/docview/1746876858
https://www.proquest.com/docview/1770360048
https://www.proquest.com/docview/1836661213
Volume 134
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