Catalytic pyrolysis of polyethylene terephthalate over zeolite catalyst: Characteristics of coke and the products

Author(s):  
Chao Li ◽  
Farshad Ataei ◽  
Farid Atashi ◽  
Xun Hu ◽  
Mortaza Gholizadeh
2018 ◽  
Vol 175 ◽  
pp. 17-25 ◽  
Author(s):  
Shuping Zhang ◽  
Houlei Zhang ◽  
Xinzhi Liu ◽  
Shuguang Zhu ◽  
Linlin Hu ◽  
...  

Author(s):  
Gorka Elordi ◽  
Gartzen Lopez ◽  
Roberto Aguado ◽  
Martin Olazar ◽  
Javier Bilbao

HDPE has been pyrolysed at 450 °C and 500 °C using HZSM-5 zeolite as a catalyst. Batch runs have been carried out at atmospheric pressure in a conical spouted bed reactor. Product analysis has been carried out by means of a GC, connected on-line with a thermostated line. The degradation rate of the plastic is slightly faster at 500 °C than at 450 °C and much faster than thermal pyrolysis in both cases. Products have been grouped into five lumps: the lump of light olefins, C2-C4; light alkanes, C1-C4; the gasoline fraction, C5-C11 compounds; C11+ hydrocarbons; and the coke deposited on the catalyst. An HZSM-5 catalyst is appropriate to obtain light olefins; about 55 wt% in both cases. The yield of gasoline fraction is also considerable and although its composition is not suitable for commercial gasoline, is interesting for its use in petrochemistry. The catalyst deactivation rate is low.


2010 ◽  
Vol 24 (12) ◽  
pp. 6233-6238 ◽  
Author(s):  
Xianghai Meng ◽  
Chunming Xu ◽  
Li Li ◽  
Jinsen Gao

2020 ◽  
Author(s):  
Agus Paul Setiawan Kaban ◽  
Naufal Ghifari Rahmat ◽  
Jaka Fajar Fatriansyah

Polymers ◽  
2021 ◽  
Vol 13 (5) ◽  
pp. 702 ◽  
Author(s):  
Justas Eimontas ◽  
Nerijus Striūgas ◽  
Mohammed Ali Abdelnaby ◽  
Samy Yousef

Recently, the pyrolysis process has been adapted as a sustainable strategy to convert metallized food packaging plastics waste (MFPW) into energy products (paraffin wax, biogas, and carbon black particles) and to recover aluminum. Usually, catalysts are used in pyrolysis treatment to refine pyrolysis products and to increase their yield. In order to study the effect of a catalyst on the formulated volatile products, this work aims to study the pyrolysis behavior of MFPW in presence of catalyst, using TG-FTIR-GC–MS system. The pyrolysis experiments were conducted with ZSM-5 Zeolite catalyst with different concentrations (10, 30, and 50 wt.%) at different heating rates (5, 10, 15, 20, 25, and 30 °C/min). In addition, TG-FTIR system and GC-MS unit were used to observe and analyze the thermal and chemical degradation of the obtained volatile compounds at maximum decomposition peaks. In addition, the kinetic results of catalytic pyrolysis of ZSM-5/MFPW samples matched when model-free methods, a distributed activation energy model (DAEM), and an independent parallel reaction kinetic model (IPR) were used. The TGA-DTG results showed that addition of a catalyst did not have a significant effect on the features of the TGA-DTG curves with similar weight loss of 87–90 wt.% (without taking the weight of the catalyst into account). Meanwhile, FTIR results manifested strong presence of methane and high-intensity functional group of carboxylic acid residues, especially at high concentration of ZSM-5 and high heating rates. Likewise, GC-MS measurements showed that Benzene, Toluene, Hexane, p-Xylene, etc. compounds (main flammable liquid compounds in petroleum oil) generated catalysts exceeding 50%. Finally, pyrolysis kinetics showed that the whole activation energies of catalytic pyrolysis process of MFPW were estimated at 289 kJ/mol and 110, 350, and 174 kJ/mol for ZSM-5/MFPW samples (10, 30, and 50 wt.%, respectively), whereas DAEM and IPR approaches succeeded to simulate TGA and DTG profiles with deviations below <1.


2021 ◽  
Vol 21 (7) ◽  
pp. 4121-4124
Author(s):  
Young-Kwon Park ◽  
Se Jeong Lim ◽  
Muhammad Zain Siddiqui ◽  
Jong-Ki Jeon ◽  
Kyung-Seun Yoo ◽  
...  

This study evaluated the feasibility of low-cost nanoporous catalysts, such as dolomite and red mud, on the production of aromatic hydrocarbons via the catalytic pyrolysis of polyethylene terephthalate (PET). Compared to the non-catalytic pyrolysis of PET, catalytic pyrolysis over both dolomite and red mud produced larger amounts of aromatic hydrocarbons owing to their catalytic cracking efficiency and decarboxylation efficiency. Between the two catalysts, red mud, having a larger BET surface area and higher basicity than dolomite, showed higher efficiency for the production of aromatic hydrocarbons.


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