TY - JOUR
T1 - Thermal degradation of acrylonitrile-butadiene-styrene (ABS) containing flame retardants using a fluidized bed reactor
T2 - The effects of Ca-based additives on halogen removal
AU - Jung, Su Hwa
AU - Kim, Seon Jin
AU - Kim, Joo Sik
PY - 2012/4
Y1 - 2012/4
N2 - In this study, the thermal degradation of a waste fraction of acrylonitrile-butadiene-styrene containing brominated flame retardants was performed to reduce halogen content in the pyrolysis oil. Thermal degradation was completed using Ca-based additives (calcium oxide, calcium hydroxide and oyster shells) in a bench-scale pyrolysis plant equipped with a fluidized bed reactor and char separation system. Pyrolysis was carried out in a temperature range of 430-510°C. In the absence of any additive, the oil yield amounted to about 77 wt.%. With the additives, the oil yield was markedly reduced to within a range of 45-64 wt.%. The principle compounds in the oils were toluene, ethylbenzene, styrene, cumene, α-methylstyrene, phenol and heteroatom-containing compounds. When Ca(OH) 2 was applied, total bromine and chlorine contents in the oil decreased to 0.05 and 0.04 wt.%, respectively. In addition, Ca(OH) 2 reduced the antimony content in the oil to below 0.001 ppm. Most of the halogens and antimony in the feed material were present in the char obtained after pyrolysis.
AB - In this study, the thermal degradation of a waste fraction of acrylonitrile-butadiene-styrene containing brominated flame retardants was performed to reduce halogen content in the pyrolysis oil. Thermal degradation was completed using Ca-based additives (calcium oxide, calcium hydroxide and oyster shells) in a bench-scale pyrolysis plant equipped with a fluidized bed reactor and char separation system. Pyrolysis was carried out in a temperature range of 430-510°C. In the absence of any additive, the oil yield amounted to about 77 wt.%. With the additives, the oil yield was markedly reduced to within a range of 45-64 wt.%. The principle compounds in the oils were toluene, ethylbenzene, styrene, cumene, α-methylstyrene, phenol and heteroatom-containing compounds. When Ca(OH) 2 was applied, total bromine and chlorine contents in the oil decreased to 0.05 and 0.04 wt.%, respectively. In addition, Ca(OH) 2 reduced the antimony content in the oil to below 0.001 ppm. Most of the halogens and antimony in the feed material were present in the char obtained after pyrolysis.
KW - Additives
KW - Dehalogenation
KW - Flame-retardant
KW - Fluidized bed
KW - Pyrolysis
UR - http://www.scopus.com/inward/record.url?scp=84862805180&partnerID=8YFLogxK
U2 - 10.1016/j.fuproc.2011.12.039
DO - 10.1016/j.fuproc.2011.12.039
M3 - Article
AN - SCOPUS:84862805180
SN - 0378-3820
VL - 96
SP - 265
EP - 270
JO - Fuel Processing Technology
JF - Fuel Processing Technology
ER -