Comparison of Components in Oil Derived from Tyre Pyrolysis with and without KL Catalyst Using GC × GC / TOF-MS
Typically, the products from waste tyre pyrolysis consist of (i) gas fraction (18 – 23 %wt ), (ii) liquid fraction (41 – 49 %wt), and (iii) char fraction (38 – 40 %wt). The liquid amount is considered the highest among those obtained from waste tyre pyrolysis. The improvements of tyre-derived oils (...
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2014-08-01
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doaj-f28af3542cd7443b9fd6a2a054cc7dd32021-02-20T21:25:50ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162014-08-013910.3303/CET1439211Comparison of Components in Oil Derived from Tyre Pyrolysis with and without KL Catalyst Using GC × GC / TOF-MSS. PithakratanayothinS. JitkarnkaTypically, the products from waste tyre pyrolysis consist of (i) gas fraction (18 – 23 %wt ), (ii) liquid fraction (41 – 49 %wt), and (iii) char fraction (38 – 40 %wt). The liquid amount is considered the highest among those obtained from waste tyre pyrolysis. The improvements of tyre-derived oils (liquid fraction) could be accomplished by increasing mono-aromatics as a result of the reductions in di-aromatics and poly- aromatics through hydrogenation and the conversion of terpenes through aromatization. A basic catalystthat has potassium as a cation such as potassium tert-butoxide (K+(CH3)3CO-)) can provide hydrogenation and aromatization. KL zeolite is a representative of a solid basic catalyst. It has a pore diameter 0.71 Åand 1-dimensional pore structure. Moreover, the 1-dimensional pore structure can align the incoming molecules parallel on the surface of KL, resulting in high yields of hydrogenated products. Two- Dimensional Gas Chromatography coupled with Time-of-Flight Mass Spectrometry (GC × GC / TOF-MS) that can separate and identify the chemicals that have same retention time and boiling points due to overlapped mass spectra was employed for better identification of components in tyre-derived oils. The objective of this research was thus to observe the changes the hydrocarbon species upon the use of a KL catalyst. The GC × GC / TOF-MS was used to investigate hydrocarbon species in the maltenes (liquid fraction without asphaltene) from the non-catalyst and KL batches. The liquid products were categorized into saturated hydrocarbons (SATs), olefins (OLEs), terpenes (TERs), mono-aromatics (MAHs), di- aromatics (DAHs), poly-aromatics (PAHs), and polar-aromatics (PPAHs), including sulphur compounds. The pyrolysis experiments were performed in a bench-scaled autoclave reactor from room temperature to 500 °C (for the pyrolysis zone) and 350 °C (for the catalytic zone) with the heating rate of 10 °C/min. As aresult, KL was found to increase the MAHs from 20.1 to 26.8 %wt (mostly, 2-ethyltetralin) and decrease DAHs form 13.31 to 6.37 %wt (mostly, 2-ethylnaphthalene), and TERs from 4.06 to 2.56 %wt (mostly, d- limonene and 3-carene). The sulphur compounds in tyre-derived oils were found to be thiophenes, phenylthiophenes, benzothiophenes, methylbenzothiophenes, dibenzothiophenes, and napthols.https://www.cetjournal.it/index.php/cet/article/view/5512 |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
S. Pithakratanayothin S. Jitkarnka |
spellingShingle |
S. Pithakratanayothin S. Jitkarnka Comparison of Components in Oil Derived from Tyre Pyrolysis with and without KL Catalyst Using GC × GC / TOF-MS Chemical Engineering Transactions |
author_facet |
S. Pithakratanayothin S. Jitkarnka |
author_sort |
S. Pithakratanayothin |
title |
Comparison of Components in Oil Derived from Tyre Pyrolysis with and without KL Catalyst Using GC × GC / TOF-MS |
title_short |
Comparison of Components in Oil Derived from Tyre Pyrolysis with and without KL Catalyst Using GC × GC / TOF-MS |
title_full |
Comparison of Components in Oil Derived from Tyre Pyrolysis with and without KL Catalyst Using GC × GC / TOF-MS |
title_fullStr |
Comparison of Components in Oil Derived from Tyre Pyrolysis with and without KL Catalyst Using GC × GC / TOF-MS |
title_full_unstemmed |
Comparison of Components in Oil Derived from Tyre Pyrolysis with and without KL Catalyst Using GC × GC / TOF-MS |
title_sort |
comparison of components in oil derived from tyre pyrolysis with and without kl catalyst using gc × gc / tof-ms |
publisher |
AIDIC Servizi S.r.l. |
series |
Chemical Engineering Transactions |
issn |
2283-9216 |
publishDate |
2014-08-01 |
description |
Typically, the products from waste tyre pyrolysis consist of (i) gas fraction (18 – 23 %wt ), (ii) liquid fraction (41 – 49 %wt), and (iii) char fraction (38 – 40 %wt). The liquid amount is considered the highest among those obtained from waste tyre pyrolysis. The improvements of tyre-derived oils (liquid fraction) could be accomplished by increasing mono-aromatics as a result of the reductions in di-aromatics and poly- aromatics through hydrogenation and the conversion of terpenes through aromatization. A basic catalystthat has potassium as a cation such as potassium tert-butoxide (K+(CH3)3CO-)) can provide hydrogenation and aromatization. KL zeolite is a representative of a solid basic catalyst. It has a pore diameter 0.71 Åand 1-dimensional pore structure. Moreover, the 1-dimensional pore structure can align the incoming molecules parallel on the surface of KL, resulting in high yields of hydrogenated products. Two- Dimensional Gas Chromatography coupled with Time-of-Flight Mass Spectrometry (GC × GC / TOF-MS) that can separate and identify the chemicals that have same retention time and boiling points due to overlapped mass spectra was employed for better identification of components in tyre-derived oils. The objective of this research was thus to observe the changes the hydrocarbon species upon the use of a KL catalyst. The GC × GC / TOF-MS was used to investigate hydrocarbon species in the maltenes (liquid fraction without asphaltene) from the non-catalyst and KL batches. The liquid products were categorized into saturated hydrocarbons (SATs), olefins (OLEs), terpenes (TERs), mono-aromatics (MAHs), di- aromatics (DAHs), poly-aromatics (PAHs), and polar-aromatics (PPAHs), including sulphur compounds. The pyrolysis experiments were performed in a bench-scaled autoclave reactor from room temperature to 500 °C (for the pyrolysis zone) and 350 °C (for the catalytic zone) with the heating rate of 10 °C/min. As aresult, KL was found to increase the MAHs from 20.1 to 26.8 %wt (mostly, 2-ethyltetralin) and decrease DAHs form 13.31 to 6.37 %wt (mostly, 2-ethylnaphthalene), and TERs from 4.06 to 2.56 %wt (mostly, d- limonene and 3-carene). The sulphur compounds in tyre-derived oils were found to be thiophenes, phenylthiophenes, benzothiophenes, methylbenzothiophenes, dibenzothiophenes, and napthols. |
url |
https://www.cetjournal.it/index.php/cet/article/view/5512 |
work_keys_str_mv |
AT spithakratanayothin comparisonofcomponentsinoilderivedfromtyrepyrolysiswithandwithoutklcatalystusinggcgctofms AT sjitkarnka comparisonofcomponentsinoilderivedfromtyrepyrolysiswithandwithoutklcatalystusinggcgctofms |
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