Co-pyrolysis coking characteristics of nC12H26 and DHN/MeOH/EtOH/MF/ DMF/H2O/H2/CO2/CO/N2 under supercritical condition

被引:1
作者
Li, Haowen [1 ,2 ]
Zhang, Hui [1 ,5 ]
Lan, Hao [1 ,4 ,6 ]
Zheng, Youdan [1 ]
Sun, Yonghui [4 ]
Lai, Zhirong [1 ]
Wang, Xiaohan [3 ,7 ]
机构
[1] Chinese Acad Sci, Ganjiang Innovat Acad, Ganzhou 341000, Peoples R China
[2] Chinese Acad Sci, Key Lab Rare Earths, Ganzhou 341000, Peoples R China
[3] Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Peoples R China
[4] Chinese Acad Sci, Inst Proc Engn, Beijing 100190, Peoples R China
[5] Univ Sci & Technol China, Sch Rare Earths, Hefei 230026, Peoples R China
[6] Chinese Acad Sci, Ganjiang Innovat Acad, 1 Kexueyuan Rd, Ganzhou 341000, Jiangxi, Peoples R China
[7] Chinese Acad Sci, Guangzhou Inst Energy Convers, 2 Nengyuan Rd, Guangzhou 510640, Guangdong, Peoples R China
基金
中国国家自然科学基金;
关键词
N-dodecane; Additive; Co -pyrolysis coking; Heat sink; Supercritical condition; HYDROGEN; CRACKING; COMBUSTION; DEPOSITION; OXIDATION; ETHYLENE; STEAM; FUEL;
D O I
10.1016/j.jaap.2024.106429
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
The introduction of additives or carrier gases to change the physicochemical process of endothermic fuel in a regenerative cooling channel and then regulate the carbon deposition behavior is an important coking control method. In this work, the co -pyrolysis and coking behavior of several novel additives, such as alcohols, furans, flue gas, and syngas, is compared under the supercritical condition of n-dodecane (nC12H26) with the traditional hydrogen supply agent decalin (DHN) and inert nitrogen (N2) as the basis in a 304STS tube with an inner diameter of 2 mm. Results show that the addition of methanol (MeOH) / ethanol (EtOH) / 2-methylfuran (MF) / 2,5-dimethylfuran (DMF) promotes the pyrolysis of nC12H26 and shows a strong coking trend. The coking rate of carbon monoxide (CO) addition is higher than that of carbon dioxide (CO2) addition, and the system is prone to presenting an exothermic chemical effect. The addition of hydrogen (H2) does not contribute to the hydrogen source but leads to a high coking risk at a low blend ratio. Although water (H2O) and CO2 atmospheres exhibit coke inhibition potential, they weaken the heat absorption capacity of nC12H26. The co -pyrolysis of alcohols, furans, and hydrocarbon feedstock to CO needs to be controlled in a targeted manner, so that endothermic fuels have high heat sink and low coking tendency in regenerative cooling channels.
引用
收藏
页数:13
相关论文
共 44 条
[1]  
Amano A, 1985, J Jap Petroleum Institute, V28, P363
[2]  
[Anonymous], 2013, CHEMKIN-PRO 15131
[3]   Experimental and Kinetic Modeling Study of 2-Methylfuran Pyrolysis at Low and Atmospheric Pressures [J].
Cheng, Zhanjun ;
He, Sirong ;
Xing, Lili ;
Wei, Lixia ;
Li, Wei ;
Li, Tianyu ;
Yan, Beibei ;
Ma, Wenchao ;
Chen, Guanyi .
ENERGY & FUELS, 2017, 31 (01) :896-903
[4]   Experimental and kinetic modeling study of 2,5-dimethylfuran pyrolysis at various pressures [J].
Cheng, Zhanjun ;
Xing, Lili ;
Zeng, Meirong ;
Dong, Weile ;
Zhang, Feng ;
Qi, Fei ;
Li, Yuyang .
COMBUSTION AND FLAME, 2014, 161 (10) :2496-2511
[5]   CO2-H2O assisted co-pyrolysis of petroleum vacuum residue and polypropylene to improve asphaltene reduction and coke suppression: A statistical approach [J].
Gharibi, Shabnam ;
Fatemi, Shohreh ;
Mjalli, Farouk S. ;
Al-Hajri, Rashid .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2023, 171
[6]   Preparation of Al2O3 coating on TiN coating by polymer-assisted deposition to improve oxidation resistance in coking inhibition applications [J].
Gong, Xianlong ;
Wang, Bo ;
Han, Huaizhi ;
Kang, Tao ;
Zhu, Quan ;
Wang, Jianli ;
Li, Xiangyuan .
CERAMICS INTERNATIONAL, 2020, 46 (06) :7774-7782
[7]   Roles of Hydrogen Donors and Organic Selenides in Inhibiting Solid Deposits from Thermal Stressing of n-Dodecane and Chinese RP-3 Jet Fuel [J].
Guo, Wei ;
Zhang, Xiangwen ;
Liu, Guozhu ;
Wang, Jing ;
Zhao, Jie ;
Mi, Zhentao .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (18) :8320-8327
[8]   Investigation of ethylene production in naphtha thermal cracking plant in presence of steam and carbon dioxide [J].
Haghighi, S. Seifzadeh ;
Rahimpour, M. R. ;
Raeissi, S. ;
Dehghani, O. .
CHEMICAL ENGINEERING JOURNAL, 2013, 228 :1158-1167
[9]   Cooling and coke deposition of hydrocarbon fuel with catalytic steam reforming [J].
Hou, Ling-Yun ;
Dong, Ning ;
Ren, Zhu-Yin ;
Zhang, Bo ;
Hu, Shen-Lin .
FUEL PROCESSING TECHNOLOGY, 2014, 128 :128-133
[10]  
Huber M., 2007, NIST THERMOPHYSICAL