electricity production cost
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2014 ◽  
Vol 30 ◽  
pp. 170-183 ◽  
Author(s):  
Simon Larsson ◽  
Dean Fantazzini ◽  
Simon Davidsson ◽  
Sven Kullander ◽  
Mikael Höök

2013 ◽  
Vol 38 (10) ◽  
pp. 3858-3864 ◽  
Author(s):  
Suat Sevencan ◽  
Tingting Guan ◽  
Göran Lindbergh ◽  
Carina Lagergren ◽  
Per Alvfors ◽  
...  

2006 ◽  
Vol 10 (3) ◽  
pp. 71-80
Author(s):  
Nikolaos Koukouzas ◽  
Paraskevas Klimantos ◽  
Prokopis Stogiannis ◽  
Emmanouel Kakaras

The aim of this paper is to examine the possibilities for the abatement of CO2 emissions in the Greek fossil fuel power generation sector. An overview of CO2 capture, transportation, and storage concepts, on which the R&D community is focused, is presented. The implementation of post-combustion CO2 capture options in an existing fossil fuel power plant is then examined and the consequences on the overall plant performance are determined. Finally, the possibilities of transportation and then underground storage of the pure CO2 stream are analyzed taking into account both technical and economical factors. The results of this analysis show that CO2 sequestration is technically feasible for existing fossil fuel fired power plants in Greece. However, substantial reduction in plant efficiency is observed due to increased energy demand of the technologies used as well as in electricity production cost due to capital and operation costs of capture, transport, and storage of CO2. .


2002 ◽  
Vol 125 (1) ◽  
pp. 365-373 ◽  
Author(s):  
M. Gambini ◽  
M. Vellini

In this paper thermodynamical and economic analyses of fossil-fuel-fired power plants, equipped with systems for CO2 recovery, are presented. The investigation has been developed with reference to power plants representative both of consolidated technology (i.e., steam cycle and combined cycle power plants), and of emerging or innovative technology (integrated coal gasification combined cycle, IGCC, and advanced mixed cycle, AMC). There are two main methods to reduce CO2 from power plant flue gas: physical and chemical absorption. In this work chemical absorption and liquefaction of CO2 removed have been considered. With reference to thermodynamical and economic performance, significant comparisons have been made between the above introduced reference plants. An efficiency decrease and an increase in the cost of electricity has been obtained when power plants are equipped with CO2 removal systems and units for liquefaction of the removed carbon dioxide. The main results of the performed investigation are quite variable among the different power plants here considered: their efficiency decreases in a range of 6 percentage points to nearly 13, while the electricity production cost increases in a range of 25% until 72%. The AMC stands out among the other power plants here analyzed because, after CO2 recovery, it exhibits the lowest net work output decrease, the highest net efficiency and the lowest final specific CO2 emission. In addition to this, its economic impact is favorable when the AMC is equipped with systems for CO2 recovery. As a result it achieves a net electric efficiency of about 50% with a carbon dioxide emission of about 0.04 kg/kWh, and the electricity production cost rises to about 25% in comparison with an AMC without CO2 removal and liquefaction systems.


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