Biomethane production from biogas obtained in wastewater treatment plants: Process optimization and economic analysis

被引:8
|
作者
Silva, J. [1 ]
Goncalves, J. C. [2 ]
Rocha, C. [2 ]
Vilaca, J. [3 ]
Madeira, L. M. [4 ]
机构
[1] Univ Porto, Dept Chem Engn, Rua Dr Roberto Frias,S-N, P-4200465 Porto, Portugal
[2] Univ Porto, Dept Chem Engn, Lab Separat & React Engn, Lab Catalysis & Mat LSRE LCM, Rua Dr Roberto Frias S-N, P-4200465 Porto, Portugal
[3] SIMDOURO, ETAR Gaia Litoral, P-4400356 Canidelo, Portugal
[4] Univ Porto, Fac Engn, Dept Chem Engn, LEPABE, Rua Dr Roberto Frias S-N, P-4200465 Porto, Portugal
关键词
Biogas; Biomethane; Methanation; Optimization; Electrolysis; Economic analysis; POWER-TO-GAS; DIRECT CATALYTIC METHANATION; OF-THE-ART; CARBON-DIOXIDE; ENERGY-STORAGE; CO2; REACTOR; HYDROGENATION; TECHNOLOGIES; ELECTROLYSIS;
D O I
10.1016/j.renene.2023.119469
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The methanation of the CO2 present in biogas is getting more and more interest, especially if hydrogen is ob-tained from renewable electricity. The biogas resulting from anaerobic digestion can be separated into CH4-and CO2-rich streams, after which the CO2 goes into the methanation section, though the biogas can also go directly into the reaction section with no separation; both alternatives were studied in this work. The two state-of-the-art methanation reactors, adiabatic and cooled fixed-bed reactors, were considered, with the latter showing a sig-nificant advantage through the formation of different reaction zones inside the reactor, allowing a simpler one -reactor approach. In this work, the use of a CH4-selective membrane was also considered to promote CO2 conversion. The results show exactly that, while the cooled reactor with no previous CO2 separation from the biogas had a CO2 conversion of 91.8 %, the adiabatic reactors showed conversions of 59.6 and 67.2 %, resulting in an overall conversion of 93.0 %. In economic terms, the scenarios studied showed negative net present worth values, considering the present conditions in Portugal and a water treatment plant as case-study, thus requiring the government to provide monetary incentives like feed-in tariffs of 0.050 euro kWh-1 for the scenarios without membrane and 0.052 euro kWh-1 for the scenarios with membrane.
引用
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页数:14
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