Issue |
E3S Web Conf.
Volume 520, 2024
4th International Conference on Environment Resources and Energy Engineering (ICEREE 2024)
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Article Number | 02024 | |
Number of page(s) | 6 | |
Section | Carbon Emission Control and Waste Resource Utilization | |
DOI | https://doi.org/10.1051/e3sconf/202452002024 | |
Published online | 03 May 2024 |
Industrial test of post combustion CO2 capture by reactive absorption with two new solvents in natural gas power plant
1 China Datang Corporation Science and Technology General Research Institute Ltd., North China Electric Power Test and Research Institute, Beijing 100040, China
2 Beijing Jingneng Power Jingyuan Thermal Power Co., Ltd., Beijing China
* Corresponding author’s e-mail: 406485892@qq.com
The post-combustion chemical decarbonization process is one of the key technology selections for the low-carbon development of natural gas power plants. The high energy consumption of amine regeneration is hindering its commercial application. In this paper, two new mixed amines solvent 15%Diethylaminoethanol (DEEA) +9% Piperazine (PZ)+ 6% Monoethanolamine (MEA) named DT01-3 and 22% 1,4-butanediamine (BDA)+ 4% N-Methyldiethanolamine (MDEA) + 4% 2-Amino-2-methyl-1-propanol (AMP) named DT02-2 are verified by the 3000Nm3/h industrial demonstration system. The steady state condition was gradually established by adjusting the main parameters such as flue gas flow rate, absorber inlet flue gas temperature, solvent circulation flow rate, regeneration tower operation pressure, steam flow rate and so on with the goal of maintaining ≥90% of the capture efficiency. The results show that the CO2 capture efficiency of DT01-3 and DT02-2 is 91.23% and 90.81% respectively. The regeneration heat consumption is 3.65 GJ/tCO2 and 3.73 GJ/tCO2. The amines consumption is 0.95kg/tCO2,1.1kg/tCO2. The operating cost of DT01-3 and DT02-2 is 336.37 CNY/t,346.04 CNY/t, which is 20.94%,18.68% lower compared with MEA.
© The Authors, published by EDP Sciences, 2024
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