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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Main Authors: S. Pithakratanayothin, S. Jitkarnka
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2014-08-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/5512
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spelling 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
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AT sjitkarnka comparisonofcomponentsinoilderivedfromtyrepyrolysiswithandwithoutklcatalystusinggcgctofms
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