Performance evaluation of a control strategy for photosynthetic biogas upgrading in a semi -industrial scale photobioreactor

被引:19
|
作者
Rodero, Maria del Rosario [1 ,2 ]
Carvajal, Andrea [1 ,3 ]
Arbib, Zouhayr [4 ]
Lara, Enrique [4 ]
de Prada, Cesar [2 ]
Lebrero, Raquel [1 ,2 ]
Munoz, Raul [1 ,2 ]
机构
[1] Univ Valladolid, Dept Chem Engn & Environm Technol, Dr Mergelina S-N, Valladolid 47011, Spain
[2] Univ Valladolid, Inst Sustainable Proc, Valladolid 47011, Spain
[3] Univ Tecn Federico Santa Maria, Dept Ingn Quim & Ambiental, Av Espana 1680, Valparaiso, Chile
[4] FCC Serv Ciudadanos, Av Camino Santiago 40,Edificio 3,4 Planta, Madrid 28050, Spain
基金
欧盟地平线“2020”;
关键词
Algal-bacterial processes; Biogas upgrading; Biomethane; Process control; Semi-industrial scale; ALGAL; MICROALGAE; TEMPERATURE; ALKALINITY; REMOVAL;
D O I
10.1016/j.biortech.2020.123207
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The validation of a control strategy for biogas upgrading via light-driven CO2 consumption by microalgae and H2S oxidation by oxidizing bacteria using the oxygen photosynthetically generated was performed in a semi-industrial scale (9.6 m(3)) photobioreactor. The control system was able to support CO2 concentrations lower than 2% with O-2 contents = 1% regardless of the pH in the cultivation broth (ranging from 9.05 to 9.50). Moreover, the control system was efficient to cope with variations in biogas flowrate from 143 to 420 L h(-1), resulting in a biomethane composition of CO2 < 2.4%, CH4 > 95.5%, O-2 < 1% and no H2S. Despite the poor robustness of this technology against failures in biogas and liquid supply (CH4 concentration of 67.5 and 70.9% after 2 h of biogas or liquid stoppage, respectively), the control system was capable of restoring biomethane quality in less than 2 h when biogas or liquid supply was resumed.
引用
收藏
页数:8
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