scholarly journals Feasibility Assessment of CO2 Capture Retrofitted to an Existing Cement Plant: Post-combustion vs. Oxy-fuel Combustion Technology

2017 ◽  
Vol 114 ◽  
pp. 6141-6149 ◽  
Author(s):  
Hana Gerbelová ◽  
Mijndert van der Spek ◽  
Wouter Schakel
2004 ◽  
Vol 126 (2) ◽  
pp. 316-321 ◽  
Author(s):  
O̸. Brandvoll ◽  
O. Bolland

In this paper an alternative to the so-called “oxy-fuel” combustion for CO2 capture is evaluated. “Chemical looping combustion” (CLC), is closely related to oxy-fuel combustion as the chemically bound oxygen reacts in a stoichiometric ratio with the fuel. In the CLC process the overall combustion reaction takes place in two reaction steps in two separate reactors. In the reduction reactor, the fuel is oxidized by the oxygen carrier, i.e., the metal oxide MeO. The metal oxide is reduced to a metal oxide with a lower oxidation number, Me, in the reaction with the fuel. In this manner, pure oxygen is supplied to the reaction with the fuel without using a traditional air separation plant, like cryogenic distillation of air. The paper presents a thermodynamic cycle analysis, where CLC is applied in a humid air turbine concept. Main parameters are identified, and these are varied to examine the influence on cycle efficiency. Results on cycle efficiency are presented and compared to other CO2 capture options. Further, an evaluation of the oxygen carrier, metals/oxides, is presented. An exergy analysis is carried out in order to understand where losses occur, and to explain the difference between CLC and conventional combustion. The oxidation reactor air inlet temperature and the oxidation reactor exhaust temperature have a significant impact on the overall efficiency. This can be attributed to the controlling effect of these parameters on the required airflow rate. An optimum efficiency of 55.9% has been found for a given set of input parameters. Crucial issues of oxygen carrier durability, chemical performance, and mechanical properties have been idealized, and further research on the feasibility of CLC is needed. Whether or not the assumption 100% gas conversion holds, is a crucial issue and remains to be determined experimentally. Successful long-term operation of chemical looping systems of this particular type has not yet been demonstrated. The simulation points out a very promising potential of CLC as a power/heat generating method with inherent capture of CO2. Exergy analysis show reduced irreversibilities for CLC compared to conventional combustion. Simulations of this type will prove useful in designing CLC systems in the future when promizing oxygen carriers have been investigated in more detail .


2014 ◽  
Vol 552 ◽  
pp. 298-303
Author(s):  
Yue Guo ◽  
Fang Qin Dai ◽  
Ni Pan

Oxygen-enriched combustion technology is an energy efficient combustion technology, which can intensify the flame stability, increase the temperature and reduce fuel consumption. Aiming at forge furnace as research object, the effects of oxygen-enriched concentration in combustion air on thermal parameters is studied. The mainly thermal parameter included the fuel combustion procedure, thermal transfer, heating time and the amount of fuel combustion. The results show that with the oxygen concentration increasing, the gas emission coefficient and radiation coefficient is higher. While the heating time, the volume of combustion air requirement, flue gas production and fuel consumption is decreased. Additionally, the study suggests that forge furnace can obtain maximize economic benefit when oxygen concentration is about 30%.


2019 ◽  
Vol 253 ◽  
pp. 113519 ◽  
Author(s):  
F. Vega ◽  
S. Camino ◽  
J.A. Camino ◽  
J. Garrido ◽  
B. Navarrete

2019 ◽  
Vol 362 ◽  
pp. 71-80 ◽  
Author(s):  
F. Vega ◽  
S. Camino ◽  
L.M. Gallego ◽  
M. Cano ◽  
B. Navarrete

Author(s):  
H. Li ◽  
J. Yan

Oxy-fuel combustion is one of promising technologies for CO2 capture, which uses simple flue gas processing normally including compression, dehydration and purification/liquefaction (non-condensable gas separation). However relatively high levels of impurities in the flu gas present more challenges for the gas processing procedure. This paper studied the sensitivity of operating parameters to inlet composition, the effects of impurities on energy consumption, and the relationship between energy consumption and operating parameters. Results show that comparatively the total compression work is more sensitive to the composition of SO2 if the total mass flow is constant; while the operating temperature of purification is more sensitive to N2. To pursue the minimum energy consumption, from the viewpoint of impurity, the content of O2, N2, Ar and H2O should be lowered as much as possible, which means the amount of air leakage into the system and excess oxygen should be controlled at a low level in the combustion; as to SO2, if it is possible to co-deposit with CO2, its existence may be helpful to decrease compression work. From the viewpoint of operating parameters, low intermediate pressure, high intercooling temperature and high outlet pressure are favorable to achieve high energy utilization, if heat recovery is considered.


2013 ◽  
Vol 1 (4) ◽  
pp. 333-343 ◽  
Author(s):  
M.Y. Han ◽  
Q. Yang ◽  
X.D. Wu ◽  
T.H. Wu ◽  
G.Q. Chen
Keyword(s):  

2017 ◽  
Vol 144 ◽  
pp. 523-539 ◽  
Author(s):  
Jana Jakobsen ◽  
Simon Roussanaly ◽  
Rahul Anantharaman
Keyword(s):  

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