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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

邮发代号 80-973

2018 Impact Factor: 3.883

Frontiers of Environmental Science & Engineering  2017, Vol. 11 Issue (5): 11   https://doi.org/10.1007/s11783-017-0998-3
  本期目录
Pyrolysis of WEEE plastics using catalysts produced from fly ash of coal gasification
Marika Benedetti1, Lorenzo Cafiero1, Doina De Angelis1, Alessandro Dell’Era2, Mauro Pasquali2, Stefano Stendardo3, Riccardo Tuffi1(), Stefano Vecchio Ciprioti2()
1. Department for Sustainability, ENEA – Casaccia Research Center, Via Anguillarese 301, S. Maria di Galeria, Rome, Italy
2. Department of SBAI, Sapienza University of Rome, Via del Castro Laurenziano 7, 00161 Rome, Italy
3. Department of Energy Technologies, ENEA – Casaccia Research Center, Via Anguillarese 301, S. Maria di Galeria, Rome, Italy
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Abstract

The effect of fly ash derived catalysts on pyrolysis of WEEE plastics was investigated.

A waste stream is recovered as a valuable resource for a new process.

Refused derived catalysts reduce the environmental impact and production costs.

Higher yields of light oil are obtained using fly ash derived catalysts.

Fly ash derived catalysts boost cracking effect and increase monoaromatics content in the oil.

Catalytic pyrolysis of thermoplastics extracted from waste electrical and electronic equipment (WEEE) was investigated using various fly ash-derived catalysts. The catalysts were prepared from fly ash by a simple method that basically includes a mechanical treatment followed by an acid or a basic activation. The synthesized catalysts were characterized using various analytical techniques. The results showed that not treated fly ash (FA) is characterized by good crystallinity, which in turn is lowered by mechanical and chemical treatment (fly ash after mechanical and acid activation, FAMA) and suppressed almost entirely down to let fly ash become completely amorphous (fly ash after mechanical and basic activation FAMB). Simultaneously, the surface area resulted increased. Subsequently, FA, FAMB and FAMA were used in the pyrolysis of a WEEE plastic sample at 400°C and their performance were compared with thermal pyrolysis at the same temperature. The catalysts principally improve the light oil yield: from 59wt.% with thermal pyrolysis to 83 wt.% using FAMB. The formation of styrene in the oil is also increased: from 243 mg/g with thermal pyrolysis to 453 mg/g using FAMB. As a result, FAMB proved to be the best catalyst, thus producing also the lowest and the highest amount of char and gas, respectively.

Key wordsWaste electrical and electronic equipment (WEEE) plastic mixture    Pyrolysis    Catalyst    Fly ash    Oil
收稿日期: 2017-05-30      出版日期: 2017-10-31
Corresponding Author(s): Riccardo Tuffi,Stefano Vecchio Ciprioti   
 引用本文:   
. [J]. Frontiers of Environmental Science & Engineering, 2017, 11(5): 11.
Marika Benedetti, Lorenzo Cafiero, Doina De Angelis, Alessandro Dell’Era, Mauro Pasquali, Stefano Stendardo, Riccardo Tuffi, Stefano Vecchio Ciprioti. Pyrolysis of WEEE plastics using catalysts produced from fly ash of coal gasification. Front. Environ. Sci. Eng., 2017, 11(5): 11.
 链接本文:  
https://academic.hep.com.cn/fese/CN/10.1007/s11783-017-0998-3
https://academic.hep.com.cn/fese/CN/Y2017/V11/I5/11
Plastic Composition
(wt.%)
ABSHIPSPBT
64.0±0.1
(from external housing)
33.0±0.1
(from external housing)
3.0±0.1
(from printed circuit board)
Elemental Analysis
(wt.%)
CHNSOClBr
85.3±0.77.8±0.13.4±0.1n.d.0.98±0.040.02±0.010.13±0.03
Proximate Analysis
(wt.%)
MoistureVolatile matterFixed CarbonAsh
0.27±0.197.0±0.91.7±0.21.9±0.2
Low Heating Value
(MJ/kg)
37.7±0.2
Tab.1  
Fig.1  
Fig.2  
Fig.3  
ExperimentLight oil (wt.%)Heavy oil (wt.%)Char (wt.%)Gas (wt.%)
Thermal59±228±213±12±1
FA67±219±212.2±0.52±1
FAMA73±26±219±22.5±0.5
FAMB83±32±111.4±0.54±2
Tab.2  
RT (min)AttributionFormulaThermalFAFAMAFAMB
2.12BenzeneC6H60.20.20.20.2
2.442-PentanoneC5H10O0.20.20.20.2
3.56TolueneC7H86.84.44.74.2
5.2EthylbenzeneC8H109.38.54.63.9
5.78StyreneC8H837.344.252.859.2
6.34Benzene, (1-methylethyl)-C9H122.13.21.40.6
7.66a-MethylstyreneC9H107.711.58.49.6
17.03BenzenebutanenitrileC10H11N11.05.16.16.7
24.79Benzene, 1,1'-(1,3-propanediyl)bis-C15H166.44.56.04.2
26.23Benzene, 1,1'-(2-butene-1,4-diyl)bis-C16H160.41.21.42.7
26.35Benzene, 1,1'-(1,2-dimethyl-1,2-ethanediyl)bis-C16H180.50.60.30.3
27.95Benzene, 1,1'-(3-methyl-1-propene-1,3-diyl)bis-C16H160.30.30.30.5
33.81Naphthalene, 1-(phenylmethyl)-C17H140.70.50.40.5
Tab.3  
Fig.4  
ExperimentH2
(%v)
CO
(%v)
CH4
(%v)
CO2
(%v)
C2H4
(%v)
C2H6
(%v)
C3H6
(%v)
C3H8
(%v)
C4H8
(%v)
C4H10
(%v)
LHV
(MJ/kg)a
Thermaln.d.18±322±136±49±16.9±0.43.6±0.21.5±0.23±20.2±0.137
FAn.d.15±211±163±36.2±0.32.2±0.11.4±0.10.4±0.10.6±0.1n.d.31
FAMAn.d.28±310±257±14±2n.d.1.2±0.10.3±0.10.7±0.2n.d.22
FAMB35±412±18±338±53.9±0.2n.d.1.6±0.20.5±0.10.5±0.1n.d.38
Tab.4  
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