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Kinetic modeling of a Claus reaction furnace and waste heat boiler: Effects of H2S/CO2 and H2S/H2O ratio on the production of hazardous gases in an industrial sulfur recovery unit
被引:3
|作者:
Ardeh, Armin Zahmatkesh
[1
]
Fathi, Sohrab
[2
]
Ashtiani, Farzin Zokaee
[1
]
Fouladitajar, Amir
[3
]
机构:
[1] Amirkabir Univ Technol, Dept Chem Engn, Tehran, Iran
[2] Kermanshah Univ Technol, Dept Chem Engn, Kermanshah, Iran
[3] Islamic Azad Univ, Dept Petr & Chem Engn, Sci & Res Branch, Tehran, Iran
关键词:
Kinetic models;
Claus process;
Reaction furnace;
Waste heat boiler;
Sulfur recovery unit;
Hazardous gases;
OPTIMIZATION;
DESTRUCTION;
HYDROGEN;
H2S;
SIMULATION;
CO2;
COMBUSTION;
DIOXIDE;
PLANT;
D O I:
10.1016/j.seppur.2023.126173
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
In this study, the reaction furnace (RF) and waste heat boiler (WHB) were modeled using a kinetic model developed from key reactions to determine how the input feed in the various acid gas scenarios affects the Sulfur Recovery Unit's (SRU's) thermal stage for industrial application. The modeling results showed that, while keeping other parameters constant, a decrease in the H2S/CO2 and H2S/H2O ratios leads to an increase in the production of hazardous gases such as CO, SO2, and COS in the Waste Heat Boiler (WHB). Consequently, this leads to a decrease in the efficiency of the Sulfur Recovery Unit (SRU). When the temperature profile is altered, the Claus reaction pathway changes unfavorably, consequently affecting the overall efficiency of the Claus process. The accuracy of the kinetic model decreases as the acid gas becomes more dilute, significantly impacting the temperature profile. The accuracy of these results was confirmed through industrial data spanning from typical acid gas to sweet gas, with a Mean Absolute Percentage Error (MAPE) ranging from 26.18 to 47.37.
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页数:11
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