Abstract

Non-thermal plasma (NTP) technologies can be used to treat a variety of gaseous pollutants, and extensive research has been carried out worldwide because of its high purification efficiency, low dependence on temperature, and other advantages. NO and SO2 are the main gaseous pollutants in coal-fired flue gas. The plasma dynamics for desulfurization and denitrification is a hot topic in the field of NTP pollutant control technologies. In this paper, a one-dimensional fluid model for the simultaneous desulfurization and denitrification of flue gas by negative direct current (DC) corona discharge was established based on the traditional zero-dimensional chemical kinetic model. The simplified wire-cylindrical electrodes configuration and numerical simulation conditions are similar to the working process of electrostatic precipitators. The results obtained by the finite element method show that the removal efficiency of NO and SO2 is remarkable in the region with a radius of less than one centimeter around the high-voltage electrode, and the effective purification area expands with the increase of the discharge voltage. There are different removal pathways for NO at different positions in the removal region, while the removal of SO2 is mainly dependent on the oxidation by OH.

Highlights

  • Non-thermal plasma (NTP) is characterized by its internal electron temperature, which is far higher than that of ions and neutral particles

  • Gas discharge at atmospheric pressure is the most common form of NTP used for flue gas treatment, such as corona discharge, dielectric barrier discharge, and so on [6,7]

  • The electron energy distribution function (EEDF) under specific gas composition can be obtained by solving the Boltzmann equation; the parameters required by the fluid model can be obtained

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Summary

Introduction

Non-thermal plasma (NTP) is characterized by its internal electron temperature, which is far higher than that of ions and neutral particles. The realization of desulfurization and denitrification relies on the highly selective chemical reactions between pollutant molecules and the active particles in plasma, which come from the collisions between high-energy electrons and background gas molecules. Teodoru et al [10] summarized the reaction path of the removal of NOx under the condition of dielectric barrier discharge in the system of NOx /N2 /O2 /H2 O, as well as the energy consumption and by-product formation with or without oxygen by solving a model consisting of 540 reactions. The chemical kinetic model and its solution, which were involved in the above studies, are essentially zero-dimensional, that is, assuming that desulfurization and denitrification are carried out in NTP with uniform spatial distribution, and ignoring the spatial characteristics of particle transport and interaction in plasma. The emphasis is laid on the analysis of the spatiotemporal evolution of desulfurization and denitrification between the discharge electrode and grounding electrode, as well as the influence of discharge voltage and background gas composition on the discharge characteristics and removal efficiency

Model Description
Governing Equations
Electron Collision and Chemical Kinetic Model
Electron Collision Kinetic Model
Chemical Kinetic Model
Collision Reactions at the Electrode Surface
Boundary Conditions
Physical Model
Mesh Generation and Numerical Solution
Results and Discussion
Effect of Discharge Voltage
Effect
Analysis
Distribution
SO oxidation of SO2 and as shown in R118
Conclusions

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