雷亚克夫
烟气脱硫
石油焦
化学
热解
噻吩
化学工程
产量(工程)
石油化工
分解
分子动力学
焦炭
有机化学
材料科学
冶金
计算化学
工程类
原子间势
作者
Jiazhuang Tian,Qiuyun Mao,Zihan You,Qifan Zhong
出处
期刊:ACS omega
[American Chemical Society]
日期:2023-05-10
卷期号:8 (20): 18140-18150
被引量:1
标识
DOI:10.1021/acsomega.3c01446
摘要
The removal of environmentally harmful S/N is crucial for utilization of high-S petroleum coke (petcoke) as fuels. Gasification of petcoke enables enhanced desulfurization and denitrification efficiency. Herein, petcoke gasification with the mixture of two effective gasifiers (CO2 and H2O) was simulated via reactive force field molecular dynamics (ReaxFF MD). The synergistic effect of the mixed agents on gas production was revealed by altering the CO2/H2O ratio. It was determined that the rise in H2O content could boost gas yield and accelerate desulfurization. Gas productivity reached 65.6% when the CO2/H2O ratio was 3:7. During the gasification, pyrolysis occurred first to facilitate the decomposition of petcoke particles and S/N removal. Desulfurization with the CO2/H2O gas mixture could be expressed as thiophene-S → S → COS → CHOS, thiophene-S → S → HS → H2S. The N-containing components experienced complicated mutual reactions before being transferred into CON, H2N, HCN, and NO. Simulating the gasification process on a molecular level is helpful in capturing the detailed S/N conversion path and reaction mechanism.
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