Next Article in Journal
Study of the Raveling Resistance of Porous Asphalt Pavements Used in Sustainable Drainage Systems Affected by Hydrocarbon Spills
Next Article in Special Issue
The Optimal Dispatch of a Power System Containing Virtual Power Plants under Fog and Haze Weather
Previous Article in Journal
Firm Sustainability Performance Index Modeling
Previous Article in Special Issue
Improving the Environmental Sustainability of Flash Geothermal Power Plants—A Case Study
Article Menu

Export Article

Open AccessArticle
Sustainability 2015, 7(12), 16213-16225; doi:10.3390/su71215811

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

1
Department for Energy Engineering, Zentralinstitut El Gouna, Technische Universität Berlin, Fraunhoferstraße 33-36, 10587 Berlin, Germany
2
Institute for Energy Engineering, Technische Universität Berlin, Marchstraße 18, 10587 Berlin, Germany
These authors contributed equally to this work.
*
Author to whom correspondence should be addressed.
Academic Editor: Andrew Kusiak
Received: 24 October 2015 / Revised: 24 November 2015 / Accepted: 1 December 2015 / Published: 4 December 2015
(This article belongs to the Special Issue Energy Conversion System Analysis)
View Full-Text   |   Download PDF [2193 KB, uploaded 4 December 2015]   |  

Abstract

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. View Full-Text
Keywords: co-production; IGCC; Methanation; substitute natural gas co-production; IGCC; Methanation; substitute natural gas
This is an open access article distributed under the Creative Commons Attribution License which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited. (CC BY 4.0).

Scifeed alert for new publications

Never miss any articles matching your research from any publisher
  • Get alerts for new papers matching your research
  • Find out the new papers from selected authors
  • Updated daily for 49'000+ journals and 6000+ publishers
  • Define your Scifeed now

SciFeed Share & Cite This Article

MDPI and ACS Style

Blumberg, T.; Sorgenfrei, M.; Tsatsaronis, G. Design and Assessment of an IGCC Concept with CO2 Capture for the Co-Generation of Electricity and Substitute Natural Gas. Sustainability 2015, 7, 16213-16225.

Show more citation formats Show less citations formats

Related Articles

Article Metrics

Article Access Statistics

1

Comments

[Return to top]
Sustainability EISSN 2071-1050 Published by MDPI AG, Basel, Switzerland RSS E-Mail Table of Contents Alert
Back to Top