scholarly journals Entrained Flow Gasification of Polypropylene Pyrolysis Oil

Molecules ◽  
2021 ◽  
Vol 26 (23) ◽  
pp. 7317
Author(s):  
Fredrik Weiland ◽  
Muhammad Saad Qureshi ◽  
Jonas Wennebro ◽  
Christian Lindfors ◽  
Taina Ohra-aho ◽  
...  

Petrochemical products could be produced from circular feedstock, such as waste plastics. Most plants that utilize syngas in their production are today equipped with entrained flow gasifiers, as this type of gasifier generates the highest syngas quality. However, feeding of circular feedstocks to an entrained flow gasifier can be problematic. Therefore, in this work, a two-step process was studied, in which polypropylene was pre-treated by pyrolysis to produce a liquid intermediate that was easily fed to the gasifier. The products from both pyrolysis and gasification were thoroughly characterized. Moreover, the product yields from the individual steps, as well as from the entire process chain, are reported. It was estimated that the yields of CO and H2 from the two-step process were at least 0.95 and 0.06 kg per kg of polypropylene, respectively, assuming that the pyrolysis liquid and wax can be combined as feedstock to an entrained flow gasifier. On an energy basis, the energy content of CO and H2 in the produced syngas corresponded to approximately 40% of the energy content of the polypropylene raw material. This is, however, expected to be significantly improved on a larger scale where losses are proportionally smaller.

Clean Energy ◽  
2020 ◽  
Vol 4 (1) ◽  
pp. 75-84
Author(s):  
Yongshi Liang ◽  
Cliff Y Guo ◽  
Xianglong Zhao ◽  
Qiang Qin ◽  
Yi Cheng ◽  
...  

Abstract A computational particle fluid dynamics simulation model for entrained-flow gasification was established in this study. The simulation results agree with the experimental data. The detailed particle information and residence-time distribution were obtained by injecting particle tracers in the simulation. The results show that the particles in the gasifier can be classified into three flowing zones, i.e. a fast-flowing zone, a recirculation zone and a spreading zone. The criterion for this classification was also provided. The rapid gas expansion caused by the fast reactions plays a significant role in forming the particle stream into these three zones. It accelerates the particles in the centre of the gasifier while pushing the particles near the expansion edge into the gas recirculation. Also, the concentrated oxygen distribution in the gasifier results in the formation of high- and low-temperature regions. The particles in the fast-flowing zone flow directly through the high-temperature region and most of these particles in this zone were fully reacted with a short residence time. Since particles in the recirculation zone are in a relatively low-temperature region, most of these particles are not fully gasified, although with a long residence time. The rest of particles in the spreading zone show moderate properties between the above two zones.


2015 ◽  
Vol 79 ◽  
pp. 166-176 ◽  
Author(s):  
E.J. Leijenhorst ◽  
D. Assink ◽  
L. van de Beld ◽  
F. Weiland ◽  
H. Wiinikka ◽  
...  

2014 ◽  
Vol 875-877 ◽  
pp. 1225-1229
Author(s):  
Zhi Qiang Wu ◽  
Shu Zhong Wang ◽  
Lin Chen ◽  
Jun Zhao ◽  
Hai Yu Meng

Entrained flow gasification technology has been attracted by gasifier researchers and companies for its wide-ranging feedstock adaptability and commercial scale availability. The optimization of the entrained flow gasifier is the critical thing for the development of entrained flow gasification technology. This paper presented a three-dimensional computational fluid dynamic (CFD) simulation for a better understanding of the cold condition flow characteristic in an entrained flow gasifier. The spraying angle, diameter and injection velocity of nozzles were found to observably affect the velocity distribution and mixing condition in the entrained flow gasifier. The numerical results could provide useful information for further research on the particle track and gasification reaction and an effective process for optimizing the gasifier and nozzle.


2009 ◽  
Vol 90 (5) ◽  
pp. 629-635 ◽  
Author(s):  
Karel Svoboda ◽  
Michael Pohořelý ◽  
Miloslav Hartman ◽  
Jiří Martinec

2007 ◽  
Vol 88 (5) ◽  
pp. 451-459 ◽  
Author(s):  
Xiaolei Guo ◽  
Zhenghua Dai ◽  
Xin Gong ◽  
Xueli Chen ◽  
Haifeng Liu ◽  
...  

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