SinoGreenTech Academic Portal
Open AccessDOI: 10.12030/j.cjee.202508052Original Research

Numerical Simulation of the Performance of a Channel-Steel Baffle-Type Pre-Dust Collector for Biomass Boiler Flue Gas

Fujian Longking Co., Ltd., Longyan 364000, China; Northeastern University, Shenyang 110819, China

Read Executive PreviewQuick FAQ
Numerical Simulation of the Performance of a Channel-Steel Baffle-Type Pre-Dust Collector for Biomass Boiler Flue Gas
Graphical Abstract / Figure
Published In
Chinese Journal of Environmental Engineering
Published:January 15, 2026Edition:Vol. 20, Issue 4 • pp. 100-112Citation:YE Xinglian et al. (2026), Chinese Journal of Environmental Engineering
Impact FactorPeer-Reviewed Core
Source Journal环境工程学报

Key Takeaways & Executive Findings

  • • • Adding a flow baffle in the ash hopper and using an upper-inlet flue duct increase collection efficiency with negligible pressure drop penalty, offering a low-resistance structural optimization path. • • Flue gas velocity is a dominant factor: efficiency drops sharply then gradually with increasing velocity, while pressure drop rises steeply; design velocity should be confined to 1.0–2.0 m·s−1 to balance performance. • • Flue gas temperature variation over tens of degrees Celsius has minimal effect: both efficiency and pressure drop decrease slightly with rising temperature, indicating robust performance under typical thermal fluctuations. • • Higher dust density and coarser particle size improve collection efficiency and reduce pressure drop, while higher dust concentration increases both; the collector is best suited for high-density, high-concentration, coarse-particle applications.

Abstract

To improve the performance of pre-dust collectors in biomass boiler flue gas purification systems, a novel channel-steel baffle-type pre-dust collector was proposed to address the low collection efficiency of conventional designs. A gas-solid two-phase flow model was developed within the MP-PIC (multiphase particle-in-cell) framework and validated against physical experiments. The model simulated gas-particle motion inside the collector, systematically investigating the effects of structural modifications, flue gas conditions, and dust properties on collection efficiency and pressure drop. Results indicate that adding a flow baffle in the ash hopper and adopting an upper-inlet flue duct enhance collection efficiency with negligible impact on pressure drop. Flue gas velocity significantly influences performance: increasing velocity reduces efficiency while raising pressure drop; an optimal design velocity of 1.0–2.0 m·s−1 is recommended. Elevated flue gas temperature slightly decreases both efficiency and pressure drop, with minimal impact over a range of tens of degrees Celsius. Higher dust density and larger particle size improve collection efficiency and reduce pressure drop, whereas higher dust concentration increases both efficiency and pressure drop. The study elucidates the mechanisms by which structural and operational parameters affect pre-dust collector performance, providing theoretical guidance for designing low-resistance, high-efficiency collectors for biomass boilers.

1. Introduction

Biomass boilers are pivotal for efficient bioenergy conversion, yet their flue gas emissions pose escalating environmental and economic challenges under tightening regulations. The typical purification train places a pre-dust collector upstream to protect downstream desulfurization, dedusting, and denitrification units. Gravity settling chambers are favored for their simplicity and cost-effectiveness, but their inherently low collection efficiency limits overall system performance. Conventional designs often fail to achieve adequate dust removal, leading to accelerated wear and reduced lifespan of downstream equipment.

This study introduces a channel-steel baffle-type pre-dust collector that leverages inertial separation to enhance dust capture. Using MP-PIC numerical simulations validated against physical experiments, the research systematically evaluates how structural modifications, flue gas conditions, and dust properties influence collection efficiency and pressure drop. The findings identify specific design levers—such as ash hopper baffles and inlet duct configuration—that improve efficiency without compromising low resistance, directly addressing the bottleneck of low-efficiency pre-cleaning in biomass boiler systems.

SinoTechIntel Interactive Document Reader
Page 1–5 of Preview
100%
Download Full PDF

Loading authentic research manuscript (Pages 1–5)...

Cite This Research Paper
YE Xinglian, ZHANG Chucheng, SU Yinbiao, LAI Huicai, AN Xizhong, LIN Chunyuan (2026). Numerical Simulation of the Performance of a Channel-Steel Baffle-Type Pre-Dust Collector for Biomass Boiler Flue Gas. Chinese Journal of Environmental Engineering. https://doi.org/10.12030/j.cjee.202508052
SinoGreenTech Academic & Legal Disclaimer

Research & Educational Purpose Only: The translations, structured abstracts, analytical annotations, and data reports provided by SinoGreenTechare intended exclusively for academic research, internal corporate R&D, and educational benchmarking. They do not constitute formal engineering, chemical safety, legal, or professional advice.

Copyright & Intellectual Property Notice: Original copyright of the underlying source articles and experimental data remains with the respective authors, institutions, and original publishing journals. SinoGreenTech claims intellectual property only over its proprietary translations, analytical syntheses, and AEO structured enhancements in accordance with international fair use and academic citation principles.

Frequently Asked Questions

What is the optimal flue gas velocity range for this pre-dust collector design, and how does velocity affect efficiency and pressure drop?

The recommended design velocity is 1.0–2.0 m·s−1. Within this range, collection efficiency remains acceptable while pressure drop is manageable. Increasing velocity beyond this range causes efficiency to drop sharply initially then gradually, while pressure drop rises steeply, making higher velocities impractical.

How do structural modifications like the ash hopper baffle and upper-inlet duct influence performance quantitatively?

Adding a flow baffle in the ash hopper and adopting an upper-inlet flue duct both improve collection efficiency with negligible impact on pressure drop. The study indicates these changes are beneficial for achieving low-resistance, high-efficiency operation, though exact percentage improvements are not specified in the provided text.

What is the effect of flue gas temperature on collector performance over a typical operating range?

Over a range of tens of degrees Celsius, flue gas temperature has minimal impact. Both pressure drop and collection efficiency decrease slightly with rising temperature, but the effect is small, ensuring stable performance under normal thermal fluctuations.

How do dust properties such as density, concentration, and particle size distribution affect the collector's efficiency and pressure drop?

Higher dust density and larger particle size improve collection efficiency and reduce pressure drop. Conversely, higher dust concentration increases both efficiency and pressure drop. The collector is particularly effective for applications with high dust density, high concentration, and a larger proportion of coarse particles.

What is the industrial significance of the MP-PIC simulation approach used in this study?

The MP-PIC method accurately captures gas-solid interactions and particle dynamics, validated against physical experiments. This enables reliable prediction of collector performance under various conditions, facilitating design optimization without costly physical prototyping, which is crucial for industrial-scale applications.

Related Chinese Research & Cross-Citations

Research Citation2026
Analysis of National and Local Policies for Medical Waste Treatment and Disposal in China

Analysis of National and Local Policies for Medical Waste Treatment and Disposal in China

The escalating generation of medical waste, driven by healthcare expansion and frequent medical activities, poses significant environmental and public health risks. Under the framework of ecological civilization, China is developing a comprehensive policy system for medical waste treatment and disposal, yet the current framework remains nascent and exhibits inconsistencies between national and local policies. This study systematically analyzes the status of national and local policies from 2003 to 2024, collecting 413 policy documents (166 from national ministries and 247 from provincial governments). The analysis examines temporal evolution, regional distribution, and policy focus, alongside the influence of medical waste output, treatment technologies, facility infrastructure, and major epidemic responses. Findings reveal distinct policy phases: initial self-disposal, exploratory management, foundational system building, and rapid development. Regional disparities are pronounced, with eastern coastal areas showing more advanced policies due to greater technical and financial resources. The surge in medical waste, particularly during the COVID-19 pandemic, underscores the need for enhanced regulatory guidance. Non-incineration technologies are gaining traction for their environmental and cost benefits, and facility coverage has improved but remains uneven. The study proposes five policy principles to foster technological innovation and industrial upgrading, ensuring safe medical waste management and environmental protection.

Examine Full Data & PDF
Research Citation2026
Kinetic Analysis and Simulation of Pollutant Removal in Sewage Networks

Kinetic Analysis and Simulation of Pollutant Removal in Sewage Networks

This study investigates pollutant removal characteristics and kinetic behaviors in sewage networks, and analyzes their impact on the carbon-to-nitrogen ratio (C/N, as COD/TN) of influent to wastewater treatment plants. Source water quality sampling at drainage outlets revealed spatial and temporal variations in C/N, with domestic sewage exhibiting higher C/N than industrial sewage, and diurnal peaks reaching 6.92 versus 4.71 during off-peak hours. Using a pilot-scale adjustable sewage network system in Kunshan, experiments were conducted under high (0.491 m·s−1) and low (0.089 m·s−1) flow velocities, monitoring pollutant removal over 144 hours. Pseudo-first-order kinetics were applied to model COD and TN removal. Results showed that COD (including SCOD and PCOD), BOD5, and SS achieved approximately 80% removal within 144 h, with higher removal at low flow velocity. TN, NH3-N, and TP exhibited lower overall removal rates. Kinetic fitting revealed that COD removal rate constants (kCOD) were significantly higher than those for TN (kTN), and both decreased with increasing flow velocity: at low velocity, kCOD=0.0167 h−1 and kTN=0.0029 h−1; at high velocity, kCOD=0.0127 h−1 and kTN=0.0020 h−1. Simulations based on actual source pollutant concentrations indicated that the time for C/N to drop to the denitrification critical value of 4.50 was 12.24 h at high velocity, but shortened to 9.49 h at low velocity. These findings demonstrate that increasing flow velocity effectively retards the decline of C/N. Therefore, regulating network flow velocity to reduce hydraulic retention time is a key strategy for maintaining adequate C/N at the terminal and ensuring denitrification efficiency in wastewater treatment plants.

Examine Full Data & PDF
Research Citation2026
Preparation of Trimetallic-Carbon Composite Catalysts and Their Application in Catalytic Ozonation of Industrial Wastewater

Preparation of Trimetallic-Carbon Composite Catalysts and Their Application in Catalytic Ozonation of Industrial Wastewater

Advanced oxidation processes (AOPs) are promising for degrading organic pollutants in water treatment. Heterogeneous catalytic ozonation (HCO) has gained attention due to its high oxidation efficiency, strong interference resistance, and low secondary pollution. In this study, a series of trimetallic-carbon composite ozone catalysts were prepared via an organic precursor calcination method using γ-Al2O3 as support. This method enhanced catalytic activity and mechanical strength while overcoming the limitations of carbon materials (low mechanical strength) and metal-based materials (poor mass transfer). The optimized catalyst, CA-FeCoCu, comprising Fe, Co, Cu, carbon, and alumina, exhibited excellent performance in phenol degradation and real industrial wastewater treatment. Characterization revealed that the synergistic effect of trimetals and the introduction of multiple carbon types increased specific surface area and hydroxyl radical (·OH) generation. In a pilot-scale fixed-bed reactor, the CA-FeCoCu/O3 system reduced COD from 120 mg·L−1 to below 40 mg·L−1, with an O3 consumption ratio (O/C) of less than 1, effectively lowering operational costs. This work provides a new strategy for developing efficient and stable heterogeneous O3 catalysts and offers a reference for the practical application of HCO in industrial wastewater treatment.

Examine Full Data & PDF
Research Citation2026
Differentiated Characteristics of Suspended Particulate Matter and Their Effects on Water Quality in the Middle and East Routes of the South-to-North Water Diversion Project

Differentiated Characteristics of Suspended Particulate Matter and Their Effects on Water Quality in the Middle and East Routes of the South-to-North Water Diversion Project

This study investigates the spatiotemporal differentiation of suspended particulate matter (SPM) characteristics, sources, and their impacts on water quality between the Middle Route (closed artificial channel) and East Route (open natural water system) of the South-to-North Water Diversion Project. Thirty sampling sites (13 on the Middle Route, 17 on the East Route) were established, and samples were collected during dry and wet seasons. Water quality parameters and SPM characteristics were analyzed, including particle size distribution, total suspended solids (TSS), chlorophyll a, and stable carbon and nitrogen isotopes. Results show that the Middle Route maintains good and stable water quality, with SPM dominated by coarse particles (>63 μm, 61.43%–94.68%), total phosphorus (TP) <0.01 mg·L−1, and a significant positive correlation between chlorophyll a and coarse particles (r=0.60), indicating algal aggregation dominates particle formation. In contrast, the East Route exhibits high and fluctuating nitrogen and phosphorus concentrations, with SPM dominated by fine particles (<20 μm, 51.26%–88.61%), TP ranging from 0.03 to 1.11 mg·L−1, and a positive correlation with fine particles, suggesting significant external inputs. Carbon and nitrogen isotope analysis reveals that Middle Route SPM primarily originates from autochthonous algae (contribution >46.75%), while East Route SPM is influenced by both terrestrial C3 plants and algae. The distinct engineering and management approaches of the two routes lead to significant differences in SPM characteristics and sources, thereby affecting water quality dynamics. The Middle Route requires an 'algal reduction and hydrodynamic optimization' strategy to control algal-derived coarse particle deposition, whereas the East Route benefits from 'retention-sedimentation and wetland purification' to reduce external fine particles and pollutant inputs. This research provides theoretical support and practical guidance for differentiated SPM management in long-distance water diversion systems.

Examine Full Data & PDF
Research Citation2026
Combined Ozone Micro-Nano Bubble Oxidation and Powdered Activated Carbon Adsorption for Removal of Taste and Odor Compounds from Drinking Water

Combined Ozone Micro-Nano Bubble Oxidation and Powdered Activated Carbon Adsorption for Removal of Taste and Odor Compounds from Drinking Water

Algal-derived taste and odor compounds (2-methylisoborneol, 2-MIB, and geosmin, GSM) in drinking water sources are poorly removed by conventional treatment. This study systematically evaluated the standalone and combined performance of ozone micro-nano bubbles (O3-MNBs) oxidation and powdered activated carbon (PAC) adsorption for removing 2-MIB, GSM, and algal cells from source water. Results showed that O3-MNBs pre-oxidation achieved >97.5% removal of odorants at 400 ng·L−1 and 67.2% algal cell removal within 30 min. When applied as a deep treatment stage, the degradation rate constant (k) was 10.1%–25.6% higher than in pre-oxidation due to lower background matrix interference. Both pre-oxidation and deep treatment reduced effluent concentrations of 2-MIB and GSM to below 10 ng·L−1, with oxidation kinetics fitting pseudo-first-order models (R²>0.95). PAC adsorption of both compounds followed pseudo-second-order kinetics (R²>0.99), with GSM equilibrium adsorption capacity approximately 20.0% higher than that of 2-MIB. In pure water, adsorption capacity increased by >10.0% compared to raw water. Based on kinetic models, a quantitative prediction method was established for O3-MNBs oxidation and PAC adsorption processes, aiming to achieve efficient odorant removal and cost optimization, providing theoretical support for advanced drinking water purification and smart water plant construction.

Examine Full Data & PDF
Research Citation2026
Pulsed Electric Field Enhancement of Nitrogen Removal Performance and Microbial Community Structure Response in Anammox Granular Sludge

Pulsed Electric Field Enhancement of Nitrogen Removal Performance and Microbial Community Structure Response in Anammox Granular Sludge

This study investigated the effects of a ring-shaped pulsed electric field (PEF) (1.5 V, 4 h on-time per cycle) on nitrogen removal performance and microbial community structure of anammox granular sludge (AnGS). Two anaerobic sequencing batch reactors (R1 control, R2 with PEF) were operated under stepwise increasing nitrogen loading rates (NLR). At NLR below 1,155 mg·(L·d)−1, R2 exhibited total nitrogen removal efficiency (TRE) 7.5%–17.0% higher than R1, with biomass, specific anammox activity (SAA), and extracellular polymeric substances (EPS) increased by 5%–7%, 21%–71%, and 54%–77%, respectively. However, at NLR above 1,320 mg·(L·d)−1, the toxic effect of nitrite dominated, and PEF enhancement diminished or even reversed to inhibition. Microbial community analysis revealed that at low-to-moderate NLR, PEF increased the relative abundance of Planctomycetes and key anammox bacteria (Candidatus Brocadia and Candidatus Jettenia), along with enhanced community richness (Chao1) and diversity (Shannon/Simpson indices). At high NLR, PEF decreased microbial richness compared to R1. Principal component analysis and redundancy analysis indicated that PEF was the key factor driving community differences at low-to-moderate NLR, whereas nitrite concentration became the dominant factor at high NLR. This study provides theoretical support for enhancing the resilience and engineering application of anammox processes.

Examine Full Data & PDF