Numerical study of co-firing coal and Cynara cardunculus in a 350 MWe utility boiler

2009 ◽  
Vol 90 (10) ◽  
pp. 1207-1213 ◽  
Author(s):  
Javier Pallarés ◽  
Antonia Gil ◽  
Cristóbal Cortés ◽  
Carlos Herce
2016 ◽  
Vol 94 ◽  
pp. 657-669 ◽  
Author(s):  
Srdjan Belošević ◽  
Ivan Tomanović ◽  
Nenad Crnomarković ◽  
Aleksandar Milićević ◽  
Dragan Tucaković

Author(s):  
Aleksandar Milićević ◽  
Srdjan Belošević ◽  
Nenad Crnomarković ◽  
Ivan Tomanović ◽  
Andrijana Stojanović ◽  
...  

2021 ◽  
pp. 411-421
Author(s):  
Qinqin Feng ◽  
Chang’an Wang ◽  
Pengqian Wang ◽  
Zhichao Wang ◽  
Wei Yao ◽  
...  

2017 ◽  
Vol 31 (5) ◽  
pp. 5344-5354 ◽  
Author(s):  
Debo Li ◽  
Qiang Lv ◽  
Yongxin Feng ◽  
Chang’an Wang ◽  
Xuan Liu ◽  
...  

Author(s):  
Iva´n F. Galindo-Garci´a ◽  
Ana Karenina Va´zquez Barraga´n ◽  
Miguel Rossano Roma´n

A computational model is developed in order to analyze flow, temperature and species distributions inside a 350 MW utility boiler. It is assumed that identification of high temperature or high velocity zones will help in the prevention of failures in the boiler walls, superheaters, reheaters and economizers. For the analysis of these failures the modeling of the chemical and physical phenomena inside the boiler is important, because one of the known causes of tube failure is the non-uniform heating of the tubes, which strongly depends on the combustion gases flow and temperature distributions. The 3-D computational fluid dynamics (CFD) codes provide an effective tool for this type of calculations. CFD calculations were performed for the condition of 100% of total load for a 350 MW utility boiler using either pulverized coal or heavy oil as fuels. The CFD calculations adopt a 3D-formulation of the mean flow equations in combination with the standard high-Reynolds-number k-epsilon turbulence model and a probability density function to model fuel combustion. The tube banks are represented by a porous media model. Comparisons between calculations and key global parameters from the power plant show relatively good agreement. Velocity profiles show a very complex flow in the boiler, especially in the lower part of the boiler, where the injected streams form a cyclone at the center of the boiler.


Fuel ◽  
2008 ◽  
Vol 87 (15-16) ◽  
pp. 3331-3338 ◽  
Author(s):  
Srdjan Belosevic ◽  
Miroslav Sijercic ◽  
Dragan Tucakovic ◽  
Nenad Crnomarkovic

2013 ◽  
Vol 732-733 ◽  
pp. 258-264
Author(s):  
Qing Xi Cao ◽  
Hui Liu ◽  
Shao Hua Wu ◽  
Wen Yan Wu ◽  
Sui Ying Yu ◽  
...  

To provide a theoretical guidance for the application of selective non-catalytic reduction (SNCR) in a large capacity utility boiler, numerical study of SNCR process in a 600 MW utility boiler was performed based on computational fluid dynamics (CFD) code Fluent. Good agreement of the calculation results with the industrial test data confirms the reliability of the calculation model. It is found that the NO removal efficiency is low and NH3-slip is high, because the injected reducing agent could not mix with the flue gas adequately, and the furnace temperature is not uniform in utility boiler with large furnace size. Aiming at this problem, the commissioning scheme for reducing agent injection system was optimized, and CO was added together with the reducing agent. As a result, NO removal efficiency increases from 19% to 27%, and NH3-slip decreases from 59 ppm to 13 ppm.


2017 ◽  
Vol 105 ◽  
pp. 4009-4014 ◽  
Author(s):  
Debo Li ◽  
Xuan Liu ◽  
Chang’an Wang ◽  
Kai Xu ◽  
Qiongliang Zha ◽  
...  

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