Partition of Cu and Pb in a Two-Stage Fluidized-Bed Waste Gasification System
In this study, a two-stage fluidized-bed gasification system was used to determine the distribution of heavy metal contaminants in simulative waste and evaluate the effect of the bed operating temperature, Equivalence ratio (ER), and Steam/Biomass ratio (S/B) in stage 1. The heavy metal concentratio...
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doaj-df6930b6f1f048378e78f7f2773bc0202020-11-24T22:19:07ZengMDPI AGApplied Sciences2076-34172019-04-0198157610.3390/app9081576app9081576Partition of Cu and Pb in a Two-Stage Fluidized-Bed Waste Gasification SystemChiou-Liang Lin0Jing-Dong Chou1Wang-Chang Weng2Department of Civil and Environmental Engineering, National University of Kaohsiung, Kaohsiung 811, TaiwanEnvironmental Protection Bureau, Kaohsiung City Government, Kaohsiung 833, TaiwanDepartment of Civil and Environmental Engineering, National University of Kaohsiung, Kaohsiung 811, TaiwanIn this study, a two-stage fluidized-bed gasification system was used to determine the distribution of heavy metal contaminants in simulative waste and evaluate the effect of the bed operating temperature, Equivalence ratio (ER), and Steam/Biomass ratio (S/B) in stage 1. The heavy metal concentrations in bed materials and fly ash were measured in two stages. The results show that as the operating temperature of stage 1 increased, the quantity of heavy metals entrapped by stage 1 bed material decreased, while that captured by stage 2 bed material increased. The less volatile Cu was mostly entrapped in stage 1 bed material. The ER and S/B results show that increasing the ER and S/B caused a slight increase in the concentrations of heavy metals entrapped in stage 1 and stage 2 bed materials. However, the influences of ER and S/B were less than that of temperature. The major factors affecting the heavy metal distribution were the operating temperature and the heavy metal volatility. Stage 2 bed material was able to entrap gaseous heavy metals or particles containing heavy metals by particle filtration and chemical adsorption. Thus, the heavy metals (Cu and Pb) had a downward trend after passing through stage 2.https://www.mdpi.com/2076-3417/9/8/1576two-stage gasifierheavy metalwastesyngaspollutant |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Chiou-Liang Lin Jing-Dong Chou Wang-Chang Weng |
spellingShingle |
Chiou-Liang Lin Jing-Dong Chou Wang-Chang Weng Partition of Cu and Pb in a Two-Stage Fluidized-Bed Waste Gasification System Applied Sciences two-stage gasifier heavy metal waste syngas pollutant |
author_facet |
Chiou-Liang Lin Jing-Dong Chou Wang-Chang Weng |
author_sort |
Chiou-Liang Lin |
title |
Partition of Cu and Pb in a Two-Stage Fluidized-Bed Waste Gasification System |
title_short |
Partition of Cu and Pb in a Two-Stage Fluidized-Bed Waste Gasification System |
title_full |
Partition of Cu and Pb in a Two-Stage Fluidized-Bed Waste Gasification System |
title_fullStr |
Partition of Cu and Pb in a Two-Stage Fluidized-Bed Waste Gasification System |
title_full_unstemmed |
Partition of Cu and Pb in a Two-Stage Fluidized-Bed Waste Gasification System |
title_sort |
partition of cu and pb in a two-stage fluidized-bed waste gasification system |
publisher |
MDPI AG |
series |
Applied Sciences |
issn |
2076-3417 |
publishDate |
2019-04-01 |
description |
In this study, a two-stage fluidized-bed gasification system was used to determine the distribution of heavy metal contaminants in simulative waste and evaluate the effect of the bed operating temperature, Equivalence ratio (ER), and Steam/Biomass ratio (S/B) in stage 1. The heavy metal concentrations in bed materials and fly ash were measured in two stages. The results show that as the operating temperature of stage 1 increased, the quantity of heavy metals entrapped by stage 1 bed material decreased, while that captured by stage 2 bed material increased. The less volatile Cu was mostly entrapped in stage 1 bed material. The ER and S/B results show that increasing the ER and S/B caused a slight increase in the concentrations of heavy metals entrapped in stage 1 and stage 2 bed materials. However, the influences of ER and S/B were less than that of temperature. The major factors affecting the heavy metal distribution were the operating temperature and the heavy metal volatility. Stage 2 bed material was able to entrap gaseous heavy metals or particles containing heavy metals by particle filtration and chemical adsorption. Thus, the heavy metals (Cu and Pb) had a downward trend after passing through stage 2. |
topic |
two-stage gasifier heavy metal waste syngas pollutant |
url |
https://www.mdpi.com/2076-3417/9/8/1576 |
work_keys_str_mv |
AT chioulianglin partitionofcuandpbinatwostagefluidizedbedwastegasificationsystem AT jingdongchou partitionofcuandpbinatwostagefluidizedbedwastegasificationsystem AT wangchangweng partitionofcuandpbinatwostagefluidizedbedwastegasificationsystem |
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