Oxygen Production for Oxy-fuel Combustion

2018 ◽  
pp. 263-287 ◽  
Author(s):  
Cong Luo ◽  
Jing Liu
RSC Advances ◽  
2015 ◽  
Vol 5 (50) ◽  
pp. 39785-39790 ◽  
Author(s):  
Qiuwan Shen ◽  
Ying Zheng ◽  
Cong Luo ◽  
Ning Ding ◽  
Chu-Guang Zheng ◽  
...  

Oxy-fuel combustion is one of the proposed technologies which have the potential to achieve zero CO2 emission.


2009 ◽  
Vol 32 (1) ◽  
pp. 127-138
Author(s):  
H. Katalambula

Carbon dioxide, a dominating contributor to global warming is emitted to the atmosphere from power plantsduring combustion of coal. Oxy-fuel combustion is a new technology leading to a simplified sequestrationof CO2. In this technology, fossil fuel is combusted with oxygen (instead of air) in such a way that the fluegas primarily consists of CO2, which can then be sequestered without significant processing. Part of the fluegas is used to dilute the oxygen in order to maintain the temperatures in the combustion process. The mainenergy penalty in oxy-fuel combustion is the cost of oxygen production. There are three major processes forair separation to produce oxygen, these are: cryogenic distillation, membrane separation and gas adsorption.Cryogenic distillation is well established process for large scale production but high energy consumption isthe main disadvantage of this process. Membrane and adsorption processes are common for small and mediumscale production. In gas adsorption, there are air separation techniques such as pressure and temperatureswing methods. The production of oxygen with 90-95% purity and 5000+tpd production is the main challengefor this technology. At present the technology that can supply oxygen in large quantity is the cryogenicseparation of oxygen from air. The papers aims at presenting a comprehensive review of the air separationtechnologies and identify areas that need attention so that oxy-firing can be achieved. The paper thereforelooks at different technologies used for oxygen production, economic concepts as well as integration issues inthe existing plants.


2021 ◽  
Author(s):  
Francisco Arnau ◽  
Ricardo Novella ◽  
Luis Miguel García-Cuevas ◽  
Fabio Gutiérrez

Abstract In transport applications, reciprocating internal combustion engines still have important advantages in terms of endurance and refueling time and available infrastructure when compared against fuel cell or battery-based powertrains. Although conventional internal combustion engine configurations produce important amounts of greenhouse gases and pollutant emissions, oxyfuel combustion can be used to mitigate to a great extent such emissions, mainly producing NOx-free, CO2 and H2O exhaust gases. However, the oxygen needed for the combustion, which is mixed with flue gases before entering the cylinder, has to be stored in an additional tank, which hinders the adoption of this technology. Fortunately, the latest developments in gas separation membranes are starting to produce extremely-high selectivity and high permeability oxygen-separation membranes. Using the waste heat of the exhaust gases to heat up a mixed ionic-electronic conducting membrane, and feeding it with pressurized air, it is possible to produce all the oxygen needed by the combustion process while keeping the whole system compact. This works presents a design of an oxy-fuel combustion engine with in-situ oxygen production. The numerical simulations show also that this concept keeps a competitive brake specific fuel consumption, while the high concentration of CO2 in the exhaust gases facilitates the introduction of carbon sequestration technologies, leading to potentially carbon-neutral internal combustion engines.


2014 ◽  
Vol 1033-1034 ◽  
pp. 146-150 ◽  
Author(s):  
Yong Qiang Xiong ◽  
Peng Luo ◽  
Ben Hua

Oxy-fuel combustion is a leading potential technology to capture CO2. Because the oxygen production process is causing the largest power penalty in oxy-fuel combustion system, it is essential to cut down oxygen separation power penalty for capturing CO2 at low cost. This paper presents the energy consumption analysis results of air separation units with three different cycles offering for oxy-fuel combustion systems. The study shows that when the gaseous oxygen compression (GOXC) cycle is selected for pressuring oxygen product stream, the specific consumption of high pressure and low purity oxygen with triple column cycle is about 6.4-7.2% less than that of with dual column cycle. And when choosing triple column cycle for oxygen production, an air separation unit with pumped liquid oxygen (PLOX) cycle is a better option than with GOXC cycle because it helps to improve plant safety and to decrease energy consumption of high pressure oxygen products.


Author(s):  
B. S. Soroka

The article considers the role and place of water and water vapor in combustion processes with the purpose of reduction the effluents of nitrogen oxides and carbon oxide. We have carried out the complex of theoretical and computational researches on reduction of harmful nitrogen and carbon oxides by gas fuel combustion in dependence on humidity of atmospheric air by two approaches: CFD modeling with attraction of DRM 19 chemical kinetics mechanism of combustion for 19 components along with Bowman’s mechanism used as “postprocessor” to determine the [NO] concentration; different thermodynamic models of predicting the nitrogen oxides NO formation. The numerical simulation of the transport processes for momentum, mass and heat being solved simultaneously in the united equations’ system with the chemical kinetics equations in frame of GRI methane combustion mechanism and NO formation calculated afterwards as “postprocessor” allow calculating the absolute actual [CO] and [NO] concentrations in dependence on combustion operative conditions and on design of furnace facilities. Prediction in frame of thermodynamic equilibrium state for combustion products ensures only evaluation of the relative value of [NO] concentration by wet combustion the gas with humid air regarding that in case of dry air – oxidant. We have developed the methodology and have revealed the results of numerical simulation of impact of the relative humidity of atmospheric air on harmful gases formation. Range of relative air humidity under calculations of atmospheric air under impact on [NO] and [CO] concentrations at the furnace chamber exit makes φ = 0 – 100%. The results of CFD modeling have been verified both by author’s experimental data and due comparing with the trends stated in world literature. We have carried out the complex of the experimental investigations regarding atmospheric air humidification impact on flame structure and environmental characteristics at natural gas combustion with premixed flame formation in open air. The article also proposes the methodology for evaluation of the nitrogen oxides formation in dependence on moisture content of burning mixture. The results of measurements have been used for verification the calculation data. Coincidence of relative change the NO (NOx) yield due humidification the combustion air revealed by means of CFD prediction has confirmed the qualitative and the quantitative correspondence of physical and chemical kinetics mechanisms and the CFD modeling procedures with the processes to be studied. A sharp, more than an order of reduction in NO emissions and simultaneously approximately a two-fold decrease in the CO concentration during combustion of the methane-air mixture under conditions of humidification of the combustion air to a saturation state at a temperature of 325 K.


2008 ◽  
Vol 39 (1) ◽  
pp. 65-78
Author(s):  
Yu. S. Teplitskii ◽  
V. A. Borodulya ◽  
V. I. Kovenskii ◽  
E. P. Nogotov

Author(s):  
S. V. Plashykhin ◽  
T. V. Bojko ◽  
D. N. Skladannyy ◽  
Ju. A. Zaporozhets ◽  
Artem S. Safiants

Sign in / Sign up

Export Citation Format

Share Document