Pyrolysis of waste tires for oil production is an effective approach for resource utilization. To optimize the process parameters of fixed-bed pyrolysis of waste tires and clarify the product characteristics, this study employed a fixed-bed electric heating system to conduct pyrolysis experiments on waste tire chunks under a nitrogen atmosphere. The effects of pyrolysis time (1h and 2h) and pyrolysis temperature (270°C~620°C) on product yields were investigated, and the reliability of the experimental data was verified through repeated tests. Furthermore, the chemical composition of the pyrolytic oil was analyzed using gas chromatography-mass spectrometry (GC-MS), while the pyrolytic char was subjected to proximate analysis, calorific value measurement, and ash fusibility testing. The results showed that extending the pyrolysis time from 1h to 2h resulted in a limited increase in oil yield (less than 1%), indicating that the tires were essentially completely cracked within 1h. As the pyrolysis temperature increased, the oil yield first rose and then declined. The optimal pyrolysis temperature range was 440°C~460°C, under which the oil yield reached 35.2%~40.1% and the oil-to-gas ratio was 2.3~2.9. The average yield of solid products ranged from 44% to 53%, with an average steel wire content of 15.5%. After the temperature exceeded 320°C, the pyrolytic carbon black yield stabilized at 29%~34%. A total of 218 effective components were detected in the pyrolytic oil, among which 13 substances, including limonene (11.87%), ethanol, and phenol, each accounted for more than 1%. The pyrolytic carbon black had a fixed carbon content exceeding 80%, a calorific value of approximately 30 MJ/kg, and an ash melting point ranging from 1170°C to 1220°C. This study provides data support for the optimization of fixed-bed pyrolysis processes for waste tires and the graded utilization of pyrolysis products.
| Published in | Science Research (Volume 14, Issue 5) |
| DOI | 10.11648/j.sr.20261405.19 |
| Page(s) | 328-334 |
| Creative Commons |
This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited. |
| Copyright |
Copyright © The Author(s), 2026. Published by Science Publishing Group |
Waste Tires, Fixed-bed Pyrolysis, Pyrolytic Oil, Pyrolytic Carbon Black, Oil Yield, Pyrolysis Temperature, Resource Utilization
项目 | 结果 | |
|---|---|---|
元素分析(收到基,%) | C | 79.93 |
H | 6.69 | |
O | 4.44 | |
N | 0.49 | |
S | 1.67 | |
工业分析(干燥基,%) | M | 2.09 |
A | 7.56 | |
V | 59.98 | |
FC | 30.37 | |
热值(kJ/kg) | 33595.49 | |
序号 | 成分比例/% | 成分名称 |
|---|---|---|
1 | 11.87 | 柠檬油精 |
2 | 2.90 | 乙醇 |
3 | 2.28 | 苯酚 |
4 | 2.07 | 二甲基环辛二烯 |
5 | 1.69 | 二甲基八三烯 |
6 | 1.56 | 苯 |
7 | 1.49 | 喹啉 |
8 | 1.19 | 螺环烃 |
9 | 1.15 | 苯并噻唑 |
10 | 1.11 | 二氢化吡唑 |
11 | 1.10 | 双环庚烷 |
12 | 1.06 | 蛇麻烯 |
13 | 1.02 | 苯乙烯 |
项目 | 名称 | 结果 |
|---|---|---|
工业分析/% | 水分 | 0.84 |
灰分 | 14.18 | |
挥发分 | 4.49 | |
固定碳 | 80.49 | |
热值/kJ·kg-1 | 29721.92 | |
灰熔融性/°C | 变形温度 | 1172 |
软化温度 | 1224 | |
流动温度 | 1239 |
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APA Style
Fan, X., Yang, L., Chen, H. (2026). Study on Fuel Oil Production from Waste Tires via Fixed-Bed Pyrolysis. Science Research, 14(5), 328-334. https://doi.org/10.11648/j.sr.20261405.19
ACS Style
Fan, X.; Yang, L.; Chen, H. Study on Fuel Oil Production from Waste Tires via Fixed-Bed Pyrolysis. Sci. Res. 2026, 14(5), 328-334. doi: 10.11648/j.sr.20261405.19
@article{10.11648/j.sr.20261405.19,
author = {Xiaoxu Fan and Liguo Yang and Hongjian Chen},
title = {Study on Fuel Oil Production from Waste Tires via
Fixed-Bed Pyrolysis},
journal = {Science Research},
volume = {14},
number = {5},
pages = {328-334},
doi = {10.11648/j.sr.20261405.19},
url = {https://doi.org/10.11648/j.sr.20261405.19},
eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.sr.20261405.19},
abstract = {Pyrolysis of waste tires for oil production is an effective approach for resource utilization. To optimize the process parameters of fixed-bed pyrolysis of waste tires and clarify the product characteristics, this study employed a fixed-bed electric heating system to conduct pyrolysis experiments on waste tire chunks under a nitrogen atmosphere. The effects of pyrolysis time (1h and 2h) and pyrolysis temperature (270°C~620°C) on product yields were investigated, and the reliability of the experimental data was verified through repeated tests. Furthermore, the chemical composition of the pyrolytic oil was analyzed using gas chromatography-mass spectrometry (GC-MS), while the pyrolytic char was subjected to proximate analysis, calorific value measurement, and ash fusibility testing. The results showed that extending the pyrolysis time from 1h to 2h resulted in a limited increase in oil yield (less than 1%), indicating that the tires were essentially completely cracked within 1h. As the pyrolysis temperature increased, the oil yield first rose and then declined. The optimal pyrolysis temperature range was 440°C~460°C, under which the oil yield reached 35.2%~40.1% and the oil-to-gas ratio was 2.3~2.9. The average yield of solid products ranged from 44% to 53%, with an average steel wire content of 15.5%. After the temperature exceeded 320°C, the pyrolytic carbon black yield stabilized at 29%~34%. A total of 218 effective components were detected in the pyrolytic oil, among which 13 substances, including limonene (11.87%), ethanol, and phenol, each accounted for more than 1%. The pyrolytic carbon black had a fixed carbon content exceeding 80%, a calorific value of approximately 30 MJ/kg, and an ash melting point ranging from 1170°C to 1220°C. This study provides data support for the optimization of fixed-bed pyrolysis processes for waste tires and the graded utilization of pyrolysis products.},
year = {2026}
}
TY - JOUR T1 - Study on Fuel Oil Production from Waste Tires via Fixed-Bed Pyrolysis AU - Xiaoxu Fan AU - Liguo Yang AU - Hongjian Chen Y1 - 2026/09/04 PY - 2026 N1 - https://doi.org/10.11648/j.sr.20261405.19 DO - 10.11648/j.sr.20261405.19 T2 - Science Research JF - Science Research JO - Science Research SP - 328 EP - 334 PB - Science Publishing Group SN - 2329-0927 UR - https://doi.org/10.11648/j.sr.20261405.19 AB - Pyrolysis of waste tires for oil production is an effective approach for resource utilization. To optimize the process parameters of fixed-bed pyrolysis of waste tires and clarify the product characteristics, this study employed a fixed-bed electric heating system to conduct pyrolysis experiments on waste tire chunks under a nitrogen atmosphere. The effects of pyrolysis time (1h and 2h) and pyrolysis temperature (270°C~620°C) on product yields were investigated, and the reliability of the experimental data was verified through repeated tests. Furthermore, the chemical composition of the pyrolytic oil was analyzed using gas chromatography-mass spectrometry (GC-MS), while the pyrolytic char was subjected to proximate analysis, calorific value measurement, and ash fusibility testing. The results showed that extending the pyrolysis time from 1h to 2h resulted in a limited increase in oil yield (less than 1%), indicating that the tires were essentially completely cracked within 1h. As the pyrolysis temperature increased, the oil yield first rose and then declined. The optimal pyrolysis temperature range was 440°C~460°C, under which the oil yield reached 35.2%~40.1% and the oil-to-gas ratio was 2.3~2.9. The average yield of solid products ranged from 44% to 53%, with an average steel wire content of 15.5%. After the temperature exceeded 320°C, the pyrolytic carbon black yield stabilized at 29%~34%. A total of 218 effective components were detected in the pyrolytic oil, among which 13 substances, including limonene (11.87%), ethanol, and phenol, each accounted for more than 1%. The pyrolytic carbon black had a fixed carbon content exceeding 80%, a calorific value of approximately 30 MJ/kg, and an ash melting point ranging from 1170°C to 1220°C. This study provides data support for the optimization of fixed-bed pyrolysis processes for waste tires and the graded utilization of pyrolysis products. VL - 14 IS - 5 ER -