Design and Assessment of an IGCC Concept with CO2 Capture for the Co-Generation of Electricity and Substitute Natural Gas

Sustainability

Timo Blumberg¹  Max Sorgenfrei²  George Tsatsaronis² 

[1] Department for Energy Engineering, Zentralinstitut El Gouna, Technische Universität Berlin, Fraunhoferstraße 33-36, 10587 Berlin, GermanyInstitute for Energy Engineering, Technische Universität Berlin, Marchstraße 18, 10587 Berlin, Germany;

关键词: co-production;    IGCC;    Methanation;    substitute natural gas;   

DOI  :  10.3390/su71215811

来源: mdpi

【 摘 要 】

The focus of this work is on the modeling and the thermodynamic evaluation of an integrated gasification combined cycle (IGCC) for the co-production of electricity and substitute natural gas (SNG). At first, an IGCC with CO₂ capture for electricity generation is analyzed. Coal-derived syngas is conditioned in a water gas shift unit (WGS), and cleaned in an acid gas removal system including carbon capture. Eventually, the conditioned syngas is fed to a combined cycle. A second case refers to a complete conversion of syngas to SNG in an integrated commercial methanation unit (TREMP™ process, Haldor Topsøe, Kgs. Lyngby, Denmark). Due to the exothermic reaction, a gas recycling and intercooling stages are necessary to avoid catalyst damage. Based on a state-of-the-art IGCC plant, an optimal integration of the synthetic process considering off-design behavior was determined. The raw syngas production remains constant in both cases, while one shift reactor in combination with a bypass is used to provide an adequate H₂/CO-ratio for the methanation unit. Electricity has to be purchased from the grid in order to cover the internal consumption when producing SNG. The resulting heat and power distributions of both cases are discussed.

【 授权许可】

CC BY   
© 2015 by the authors; licensee MDPI, Basel, Switzerland.