Next Article in Journal
Integration of Large Scale PV-Based Generation into Power Systems: A Survey
Next Article in Special Issue
Numerical Study of the Structure and NO Emission Characteristics of N2- and CO2-Diluted Tubular Diffusion Flames
Previous Article in Journal
A Current Reconstruction Strategy Following the Operation Area in a 1-Shunt Inverter System
Previous Article in Special Issue
The Impact of Fuel Type on the Output Parameters of a New Biofuel Burner
Article Menu
Issue 8 (April-2) cover image

Export Article

Open AccessArticle

Study on Powder Coke Combustion and Pollution Emission Characteristics of Fluidized Bed Boilers

1
Key Laboratory of Low-Grade Energy Utilization Technologies and Systems, Chongqing University, Ministry of Education, Chongqing 400030, China
2
School of Energy and Power Engineering, Chongqing University, Chongqing 400030, China
3
Science and Technology on Reactor System Design Technology Laboratory, Nuclear Power Institute of China, Chengdu 610213, China
*
Author to whom correspondence should be addressed.
Energies 2019, 12(8), 1424; https://doi.org/10.3390/en12081424
Received: 22 February 2019 / Revised: 6 April 2019 / Accepted: 9 April 2019 / Published: 13 April 2019
(This article belongs to the Special Issue Cleaner Combustion)
  |  
PDF [5138 KB, uploaded 13 April 2019]
  |  

Abstract

The fluidized reactor is widely used in a number of chemical processes due to its high gas-particle contacting efficiency and excellent performance on solid mixing. An improved numerical framework based on the multiphase particle-in-cell (MP-PIC) method has been developed to simulate the processes of gas–solid flow and chemical reactions in a fluidized bed. Experiments have been carried out with a 3-MW circulating fluidized bed with a height of 24.5 m and a cross section of 1 m2. In order to obtain the relationship between pollutant discharge and operating conditions and to better guide the operation of the power plant, a series of tests and simulations were carried out. The distributions of temperature and gas concentration along the furnace from simulations achieved good accuracy compared with experimental data, indicating that this numerical framework is suitable for solving complex gas–solid flow and reactions in fluidized bed reactors. Through a series of experiments, the factors affecting the concentration of NOx and SOx emissions during the steady-state combustion of the normal temperature of powder coke were obtained, which provided some future guidance for the operation of a power plant burning the same kind of fuel. View Full-Text
Keywords: fluidized bed; powder coke; MP-PIC method; emission characteristics fluidized bed; powder coke; MP-PIC method; emission characteristics
Figures

Figure 1

This is an open access article distributed under the Creative Commons Attribution License which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited (CC BY 4.0).
SciFeed

Share & Cite This Article

MDPI and ACS Style

Yang, C.; Wu, H.; Deng, K.; He, H.; Sun, L. Study on Powder Coke Combustion and Pollution Emission Characteristics of Fluidized Bed Boilers. Energies 2019, 12, 1424.

Show more citation formats Show less citations formats

Note that from the first issue of 2016, MDPI journals use article numbers instead of page numbers. See further details here.

Related Articles

Article Metrics

Article Access Statistics

1

Comments

[Return to top]
Energies EISSN 1996-1073 Published by MDPI AG, Basel, Switzerland RSS E-Mail Table of Contents Alert
Back to Top