Catalytic Pyrolysis Mechanism of β-O-4 Type of Lignin Dimer: The Role of H Proton

2020 ◽  
Vol 35 (1) ◽  
pp. 575-582
Author(s):  
Min Chen ◽  
Weipeng Zhong ◽  
Kai Wu ◽  
Gang Wei ◽  
Zonghua Hu ◽  
...  
2020 ◽  
Vol 218 ◽  
pp. 1-11 ◽  
Author(s):  
Chuan Yuan ◽  
Ding Jiang ◽  
Shuang Wang ◽  
Bahram Barati ◽  
Xun Gong ◽  
...  

2021 ◽  

Abstract The full text of this preprint has been withdrawn by the authors as it was submitted and made public without the full consent of all the authors. Therefore, the authors do not wish this work to be cited as a reference. Questions should be directed to the corresponding author.


2021 ◽  
Author(s):  
Zeyou Pan ◽  
Allen Puente-Urbina ◽  
Andras Bodi ◽  
Jeroen A. van Bokhoven ◽  
Patrick Hemberger

Detection of reactive intermediates with synchrotron radiation and photoelectron photoion coincidence methods reveals new mechanistic insights into lignin catalytic pyrolysis. Here we focus on how the isomerism changes the conversion and product formation.


Catalysts ◽  
2019 ◽  
Vol 9 (11) ◽  
pp. 953
Author(s):  
Jianwei Liu ◽  
Qian Zhang ◽  
Litong Liang ◽  
Wei Huang

Understanding the catalytic pyrolysis mechanism of lignite is of great significance for obtaining a high yield of the target products or designing high-efficiency catalysts, which are generally derived by using simple model compounds, while the ordinary model compounds cannot represent the real atmosphere of lignite pyrolysis owing to the simple structures and single reactions. Based on the coal two-phase model, the extractable compounds are the important compositions of coal, which can reflect the partial characteristics of raw coal while obtaining a high extraction yield. Hence, a better understanding of the interaction between the coal structure and catalyst can be inferred by using a mobile phase in coal as model compounds instead of conventional simple compounds. In this work, tetrahydrofuran extracts of lignite were chosen as model compounds to study the catalytic pyrolysis mechanism with separate addition of Fe(NO3)3 and FeCl3 by using a thermogravimetric combined with mass spectrometry. It was found that about 77.88% of the extracts were vaporized before 700 °C, and the residual yield was 22.12%. With the separate addition of 5 wt % of Fe(NO3)3 and FeCl3, the conversion of the extracts increased to 84.38% and 89.66%. Meanwhile, the final temperature decreased to 650 and 550 °C, respectively. The addition of Fe(NO3)3 and FeCl3 promoted the breakage of aliphatic chains at approximately 150 °C, leading to the generation of CH4 and H2 in the temperature range 100–200 °C, which were nearly invisible for that without catalyst. The addition of iron-based catalysts allowed more CO2 formation at approximately 200 °C since they enabled efficient promotion of the cleavage of carboxyl functionals at lower temperatures. The enlarged peak of H2O and CH4 at approximately 500 °C means that iron-based catalysts are significant for the cleavage of methoxy groups in the catalytic respect. Aromatic side chains facilitated cracking at approximately 500 °C, leading to more light aliphatics and aromatics generation in this temperature range.


Catalysts ◽  
2020 ◽  
Vol 10 (6) ◽  
pp. 602 ◽  
Author(s):  
Muhammad Zain Siddiqui ◽  
Tae Uk Han ◽  
Young-Kwon Park ◽  
Young-Min Kim ◽  
Seungdo Kim

The thermal and catalytic pyrolysis of two kinds of Tetra Pak waste (TP-1 and TP-2) over three different acidic catalysts—HZSM-5(SiO2/Al2O3, 30), HBeta (38), and Al-MCM-41(20)—were investigated in this study. Tetra Pak (TP) wastes consist of composite material comprising kraft paper, polyethylene (PE) film, and aluminum foil. Thermal decomposition behaviors during the pyrolysis of TPs were monitored using a thermogravimetric (TG) analyzer and tandem micro reactor-gas chromatography/mass spectrometry (TMR-GC/MS). Neither the interaction between the non-catalytic pyrolysis intermediates of kraft paper and PE, nor the effect of aluminum foil have been monitored during the non-catalytic TG analysis of TPs. The maximum decomposition temperatures of PE in TP-1 shifted from 465 °C to 432 °C by HBeta(38), 439 °C by HZSM-5(30), and 449 °C by Al-MCM-41(20), respectively. The results of the TMR-GC/MS analysis indicate that the non-catalytic pyrolysis of TPs results in the formation of large amounts of furans and heavy hydrocarbons and they are converted efficiently to aromatic hydrocarbons over the acidic catalysts. Among the three catalysts, HZSM-5(30) produced the largest amount of aromatic hydrocarbons, followed by HBeta(38) and Al-MCM-41(20) owing to their different acidity and pore size. Compared to TP-1, TP-2 produced a larger amount of aromatic hydrocarbons via catalytic pyrolysis because of its relatively larger PE content. The synergistic formation of aromatic hydrocarbons was also enhanced during the catalytic pyrolysis of TPs due to the effective role of PE as hydrogen donor to kraft paper. In terms of their catalytic effectiveness, HZSM-5(30) had a longer lifetime than HBeta(38).


2015 ◽  
Vol 140 ◽  
pp. 119-124 ◽  
Author(s):  
Thanh Khoa Phung ◽  
Alessandro A. Casazza ◽  
Patrizia Perego ◽  
Pierlorenzo Capranica ◽  
Guido Busca

2021 ◽  
Author(s):  
Xiaoxue Cheng ◽  
Ding Jiang ◽  
Zhen Xia ◽  
Bahram Barati ◽  
Karthickeyan Viswanathan ◽  
...  

Abstract Cellulose is one of the main components of terrestrial biomass. In this study, a zeolite catalyst (ZSM-5) was used to catalyze the pyrolysis of cellulose. The components produced during pyrolysis were tested by Py-GC/MS, and the pyrolysis mechanism was analyzed by density functional theory (DFT). The results showed that furans and sugars were the primary pyrolysis products. After catalytic pyrolysis, the furfural content was significantly lower than that of non-catalytic pyrolysis. However, the yield of aromatic hydrocarbons increased significantly, especially benzene, which increased from almost zero to 13.04%. DFT further explored the specific reaction pathway of catalytic pyrolysis. It was found that under the catalysis of ZSM-5, the catalyst directly participated in most cellulose pyrolysis reactions. Also, the electrophilicity of acid sites in the reaction system played an important role. Therefore, the catalysis of the molecular sieve can significantly reduce the energy barrier of each path. In generating aromatic hydrocarbons, the decarbonylation reaction and dehydration reaction of furfural can be completely catalyzed, thereby increasing the reaction rate of generating aromatic hydrocarbons. Some deoxygenation steps occurred during the reaction, which made the catalytic pyrolysis reaction easier to develop, and improved the bio-oil quality.


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