Computational Particle Fluid Dynamics Simulation on Combustion Characteristics of Blended Fuels of Coal, Biomass, and Oil Sludge in a 130 t h<sup>−1</sup> Circulating Fluidized Bed Boiler

In this study, the co-combustion of coal and biomass, and the tri-combustion of coal, biomass, and oil sludge in a 130 t h<sup>−1</sup> circulating fluidized bed (CFB) boiler are investigated via the computational particle fluid dynamics (CPFD) approach. Furthermore, the effect of biomas...

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Main Authors: Yang Wang, Xiangyu Chen, Liping Xu, Mingwei Ma, Xiaole Huang, Feng Han, Yong Zhou, Chen Du, Yaodong Da, Lei Deng
Format: Article
Language:English
Published: MDPI AG 2023-12-01
Series:Energies
Subjects:
Online Access:https://www.mdpi.com/1996-1073/17/1/149
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author Yang Wang
Xiangyu Chen
Liping Xu
Mingwei Ma
Xiaole Huang
Feng Han
Yong Zhou
Chen Du
Yaodong Da
Lei Deng
author_facet Yang Wang
Xiangyu Chen
Liping Xu
Mingwei Ma
Xiaole Huang
Feng Han
Yong Zhou
Chen Du
Yaodong Da
Lei Deng
author_sort Yang Wang
collection DOAJ
description In this study, the co-combustion of coal and biomass, and the tri-combustion of coal, biomass, and oil sludge in a 130 t h<sup>−1</sup> circulating fluidized bed (CFB) boiler are investigated via the computational particle fluid dynamics (CPFD) approach. Furthermore, the effect of biomass feeding position is also comprehensively evaluated. The results show that for the co-combustion of coal and biomass, the O<sub>2</sub> mole fraction at the furnace outlet rises from 0.0541 to 0.0640 as the biomass blending ratio enhances from 40% to 100%, while the CO<sub>2</sub> mole fraction reduces from 0.1357 to 0.1267. The mole fraction of NO<i><sub>x</sub></i> and SO<sub>2</sub> at the furnace outlet decreases from 4.5867 × 10<sup>−5</sup> to 3.9096 × 10<sup>−5</sup> and 2.8253 × 10<sup>−4</sup> to 4.6635 × 10<sup>−5</sup>, respectively. For the tri-combustion of three fuels, the average NO<i><sub>x</sub></i> mole fraction initially grows quickly and then declines gradually, ranging from 4.1173 × 10<sup>−5</sup> to 4.2556 × 10<sup>−5</sup>. The mole fraction of SO<sub>2</sub> at the furnace outlet increases from 3.5176 × 10<sup>−4</sup> to 4.7043 × 10<sup>−4</sup> when the ratio of oil sludge rises from 10% to 20%. The uniformity of temperature and gas components distribution is “new inlet > secondary air inlet > feed inlet”. As for the three inlet positions, the mole fractions of NO<i><sub>x</sub></i> at the furnace outlet are between 3.9096 × 10<sup>−5</sup> and 5.1537 × 10<sup>−5</sup>, while those for SO<sub>2</sub> are between 2.5978 × 10<sup>−4</sup> and 2.5278 × 10<sup>−4</sup>.
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spelling doaj.art-2e804af3ca9a436b973eea6acea853ac2024-01-10T14:56:00ZengMDPI AGEnergies1996-10732023-12-0117114910.3390/en17010149Computational Particle Fluid Dynamics Simulation on Combustion Characteristics of Blended Fuels of Coal, Biomass, and Oil Sludge in a 130 t h<sup>−1</sup> Circulating Fluidized Bed BoilerYang Wang0Xiangyu Chen1Liping Xu2Mingwei Ma3Xiaole Huang4Feng Han5Yong Zhou6Chen Du7Yaodong Da8Lei Deng9Engineering Technology Research Institute (Supervision Company), PetroChina Xinjiang Oilfield Company, Karamay 834000, ChinaEngineering Technology Research Institute (Supervision Company), PetroChina Xinjiang Oilfield Company, Karamay 834000, ChinaEngineering Technology Research Institute (Supervision Company), PetroChina Xinjiang Oilfield Company, Karamay 834000, ChinaEngineering Technology Research Institute (Supervision Company), PetroChina Xinjiang Oilfield Company, Karamay 834000, ChinaState Key Laboratory of Multiphase Flow in Power Engineering, School of Energy and Power Engineering, Xi’an Jiaotong University, Xi’an 710049, ChinaEngineering Technology Research Institute (Supervision Company), PetroChina Xinjiang Oilfield Company, Karamay 834000, ChinaEngineering Technology Research Institute (Supervision Company), PetroChina Xinjiang Oilfield Company, Karamay 834000, ChinaEngineering Technology Research Institute (Supervision Company), PetroChina Xinjiang Oilfield Company, Karamay 834000, ChinaState Key Laboratory of Multiphase Flow in Power Engineering, School of Energy and Power Engineering, Xi’an Jiaotong University, Xi’an 710049, ChinaState Key Laboratory of Multiphase Flow in Power Engineering, School of Energy and Power Engineering, Xi’an Jiaotong University, Xi’an 710049, ChinaIn this study, the co-combustion of coal and biomass, and the tri-combustion of coal, biomass, and oil sludge in a 130 t h<sup>−1</sup> circulating fluidized bed (CFB) boiler are investigated via the computational particle fluid dynamics (CPFD) approach. Furthermore, the effect of biomass feeding position is also comprehensively evaluated. The results show that for the co-combustion of coal and biomass, the O<sub>2</sub> mole fraction at the furnace outlet rises from 0.0541 to 0.0640 as the biomass blending ratio enhances from 40% to 100%, while the CO<sub>2</sub> mole fraction reduces from 0.1357 to 0.1267. The mole fraction of NO<i><sub>x</sub></i> and SO<sub>2</sub> at the furnace outlet decreases from 4.5867 × 10<sup>−5</sup> to 3.9096 × 10<sup>−5</sup> and 2.8253 × 10<sup>−4</sup> to 4.6635 × 10<sup>−5</sup>, respectively. For the tri-combustion of three fuels, the average NO<i><sub>x</sub></i> mole fraction initially grows quickly and then declines gradually, ranging from 4.1173 × 10<sup>−5</sup> to 4.2556 × 10<sup>−5</sup>. The mole fraction of SO<sub>2</sub> at the furnace outlet increases from 3.5176 × 10<sup>−4</sup> to 4.7043 × 10<sup>−4</sup> when the ratio of oil sludge rises from 10% to 20%. The uniformity of temperature and gas components distribution is “new inlet > secondary air inlet > feed inlet”. As for the three inlet positions, the mole fractions of NO<i><sub>x</sub></i> at the furnace outlet are between 3.9096 × 10<sup>−5</sup> and 5.1537 × 10<sup>−5</sup>, while those for SO<sub>2</sub> are between 2.5978 × 10<sup>−4</sup> and 2.5278 × 10<sup>−4</sup>.https://www.mdpi.com/1996-1073/17/1/149tri-combustionCPFDCFB boilercombustion characteristicsNO<i><sub>x</sub></i> emission
spellingShingle Yang Wang
Xiangyu Chen
Liping Xu
Mingwei Ma
Xiaole Huang
Feng Han
Yong Zhou
Chen Du
Yaodong Da
Lei Deng
Computational Particle Fluid Dynamics Simulation on Combustion Characteristics of Blended Fuels of Coal, Biomass, and Oil Sludge in a 130 t h<sup>−1</sup> Circulating Fluidized Bed Boiler
Energies
tri-combustion
CPFD
CFB boiler
combustion characteristics
NO<i><sub>x</sub></i> emission
title Computational Particle Fluid Dynamics Simulation on Combustion Characteristics of Blended Fuels of Coal, Biomass, and Oil Sludge in a 130 t h<sup>−1</sup> Circulating Fluidized Bed Boiler
title_full Computational Particle Fluid Dynamics Simulation on Combustion Characteristics of Blended Fuels of Coal, Biomass, and Oil Sludge in a 130 t h<sup>−1</sup> Circulating Fluidized Bed Boiler
title_fullStr Computational Particle Fluid Dynamics Simulation on Combustion Characteristics of Blended Fuels of Coal, Biomass, and Oil Sludge in a 130 t h<sup>−1</sup> Circulating Fluidized Bed Boiler
title_full_unstemmed Computational Particle Fluid Dynamics Simulation on Combustion Characteristics of Blended Fuels of Coal, Biomass, and Oil Sludge in a 130 t h<sup>−1</sup> Circulating Fluidized Bed Boiler
title_short Computational Particle Fluid Dynamics Simulation on Combustion Characteristics of Blended Fuels of Coal, Biomass, and Oil Sludge in a 130 t h<sup>−1</sup> Circulating Fluidized Bed Boiler
title_sort computational particle fluid dynamics simulation on combustion characteristics of blended fuels of coal biomass and oil sludge in a 130 t h sup 1 sup circulating fluidized bed boiler
topic tri-combustion
CPFD
CFB boiler
combustion characteristics
NO<i><sub>x</sub></i> emission
url https://www.mdpi.com/1996-1073/17/1/149
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