scholarly journals Status of ClaRaCCS: Modelling and Simulation of Coal-Fired Power Plants with CO2 Capture

2012 ◽  
Author(s):  
Johannes Brunnemann ◽  
Friedrich Gottelt ◽  
Kai Wellner ◽  
Ala Renz ◽  
Andre Thüring ◽  
...  
Keyword(s):  
Co2 Capture ◽  
Power Plants ◽  
Modelling And Simulation

scholarly journals Demonstrating full-scale post-combustion CO2 capture for coal-fired power plants through dynamic modelling and simulation

Fuel ◽  
2012 ◽  
Vol 101 ◽  
pp. 115-128 ◽  
Author(s):  
Adekola Lawal ◽  
Meihong Wang ◽  
Peter Stephenson ◽  
Okwose Obi
Keyword(s):  
Co2 Capture ◽  
Power Plants ◽  
Dynamic Modelling ◽  
Full Scale ◽  
Modelling And Simulation

Life cycle cost assessment of biomass co-firing power plants with CO2 capture and storage considering multiple incentives

2021 ◽  
Vol 96 ◽  
pp. 105173
Author(s):  
Bo Yang ◽  
Yi-Ming Wei ◽  
Lan-Cui Liu ◽  
Yun-Bing Hou ◽  
Kun Zhang ◽  
...  
Keyword(s):  
Life Cycle ◽  
Co2 Capture ◽  
Life Cycle Cost ◽  
Power Plants ◽  
Cost Assessment ◽  
Co2 Capture And Storage ◽  
And Storage

Energy and Exergy Analyses of a Power Plant With Carbon Dioxide Capture Using Multistage Chemical Looping Combustion

2016 ◽  
Vol 139 (3) ◽  
Author(s):  
Bilal Hassan ◽  
Oghare Victor Ogidiama ◽  
Mohammed N. Khan ◽  
Tariq Shamim
Keyword(s):  
Carbon Dioxide ◽  
Power Plant ◽  
Natural Gas ◽  
Co2 Capture ◽  
Power Plants ◽  
Waste Heat ◽  
Chemical Looping Combustion ◽  
Chemical Looping ◽  
Operating Pressure ◽  
Efficiency Gain

A thermodynamic model and parametric analysis of a natural gas-fired power plant with carbon dioxide (CO2) capture using multistage chemical looping combustion (CLC) are presented. CLC is an innovative concept and an attractive option to capture CO2 with a significantly lower energy penalty than other carbon-capture technologies. The principal idea behind CLC is to split the combustion process into two separate steps (redox reactions) carried out in two separate reactors: an oxidation reaction and a reduction reaction, by introducing a suitable metal oxide which acts as an oxygen carrier (OC) that circulates between the two reactors. In this study, an Aspen Plus model was developed by employing the conservation of mass and energy for all components of the CLC system. In the analysis, equilibrium-based thermodynamic reactions with no OC deactivation were considered. The model was employed to investigate the effect of various key operating parameters such as air, fuel, and OC mass flow rates, operating pressure, and waste heat recovery on the performance of a natural gas-fired power plant with multistage CLC. The results of these parameters on the plant's thermal and exergetic efficiencies are presented. Based on the lower heating value, the analysis shows a thermal efficiency gain of more than 6 percentage points for CLC-integrated natural gas power plants compared to similar power plants with pre- or post-combustion CO2 capture technologies.

Multi-functional heat pumps integration in power plants for CO2 capture and sequestration

2015 ◽  
Vol 147 ◽  
pp. 258-268 ◽  
Author(s):  
Abdullah Alabdulkarem ◽  
Yunho Hwang ◽  
Reinhard Radermacher
Keyword(s):  
Co2 Capture ◽  
Power Plants ◽  
Heat Pumps ◽  
Co2 Capture And Sequestration

scholarly journals On the operability of power plants with CO2 capture and storage

2009 ◽  
Vol 1 (1) ◽  
pp. 1521-1526 ◽  
Author(s):  
Colin Alie ◽  
Peter L. Douglas ◽  
John Davison
Keyword(s):  
Co2 Capture ◽  
Power Plants ◽  
Co2 Capture And Storage ◽  
And Storage
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