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中国腐蚀与防护学报  2026, Vol. 46 Issue (4): 1148-1158     CSTR: 32134.14.1005.4537.2025.304      DOI: 10.11902/1005.4537.2025.304
  研究报告 本期目录 | 过刊浏览 |
生物质飞灰粒度与浓度对电站锅炉协同腐蚀损伤特性研究
吴健, 姚锡文(), 许开立, 许克强
东北大学资源与土木工程学院 沈阳 110819
Influence of Particle Size and Deposit Amount of Biomass Fly Ash on Corrosion Damage of Boiler Tube Steel for Biomass Power Stations
WU Jian, YAO Xiwen(), XU Kaili, XU Keqiang
School of Resources and Civil Engineering, Northeastern University, Shenyang 110819, China
引用本文:

吴健, 姚锡文, 许开立, 许克强. 生物质飞灰粒度与浓度对电站锅炉协同腐蚀损伤特性研究[J]. 中国腐蚀与防护学报, 2026, 46(4): 1148-1158.
Jian WU, Xiwen YAO, Kaili XU, Keqiang XU. Influence of Particle Size and Deposit Amount of Biomass Fly Ash on Corrosion Damage of Boiler Tube Steel for Biomass Power Stations[J]. Journal of Chinese Society for Corrosion and protection, 2026, 46(4): 1148-1158.

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摘要: 

生物质电厂锅炉运行过程中产生的飞灰颗粒沉积在金属受热面上易导致金属减薄或腐蚀泄漏,是引发电厂锅炉受热面腐蚀爆管事故频发的重要原因。为探究木材类生物质热转化过程中飞灰颗粒的沉积腐蚀损伤特性,本研究以松木屑灰为研究对象、腐蚀增重量及腐蚀产物特征为评价指标,利用基于管式炉系统自行搭建的腐蚀实验平台模拟研究烟气温度为600 ℃且主要气体组分为CO2、O2和N2的典型锅炉烟气环境中,不同粒径颗粒(< 30、30~75和75~100 μm)和不同涂灰量(10、20和30 mg/cm2)对我国生物质电厂锅炉典型常用钢材12Cr1MoVG高温腐蚀特性的影响规律及作用机理。结果表明,木屑灰颗粒诱导锅炉受热面金属腐蚀效应受颗粒粒度与积灰量的协同作用影响显著,不同粒径颗粒对金属受热面高温腐蚀的调控呈现出不同的作用效果:当涂灰量为10 mg/cm2时,75~100 μm的大颗粒因比表面积相对较小导致烧结迟缓,持续释放活性组分且灰层孔隙疏松,促进局部腐蚀;而粒径为30~75 μm的颗粒在20 mg/cm2的涂灰量下,可以通过分级孔隙结构形成加速腐蚀的协同效应;但是当涂灰量增至30 mg/cm2时,不同粒径颗粒物均因灰层的孔隙率较低而呈现腐蚀抑制作用;在本实验工况下,当颗粒粒径为75~100 μm且涂灰量为10 mg/cm2时腐蚀现象最显著,其次为30~75 μm且涂灰量为20 mg/cm2情形,而当颗粒粒径< 30 μm时,腐蚀现象在20 mg/cm2时最显著。研究成果可为揭示生物质电厂锅炉不同粒径颗粒物诱导受热面高温腐蚀特性及机理提供科学指导。

关键词 : 碱金属腐蚀,  积灰腐蚀,  颗粒粒度,  涂灰量,  腐蚀爆管    
Abstract:

Fly ash particles, generated during the operation of biomass power plant boilers, deposited on the surface of metallic heating components are likely to cause metal thinning or corrosion leakage, which is an important cause for the frequent occurrence of corrosion and tube-bursting accidents of the metallic heating components for the power plant boilers. Herein, the effect of particles of different sizes (< 30, 30-75 and 75-100 μm) and different deposit amount (10, 20, and 30 mg/cm2) of pine wooden chip ash on the surface of 12Cr1MoVG steel, a typical common steel used for boilers of biomass power plants in the country, on the high-temperature corrosion behavior of the steel was investigated via a home-made set of a tube-furnace system to simulate typical boiler flue-gas composed of CO2, O2 and N2 at 600 ℃, as well as per weight change measurement and relevant characterization techniques for corrosion products, in terms of the corrosion mechanism of the boiler tube steel induced by fly ash deposits generated during wooden biomass combustion. The results show that the influence of wooden ash particles on the corrosion of the boiler tube steel surface is determined by the particle size of the fly ash and its deposition amount. Namely, for the cumulative ash deposition amount is 10 mg/cm2 and their particles range within 75-100 μm (large particles), due to their relatively small specific surface area, they are not prone to agglomeration, therewith the ash deposits present a loose and pore structure, which may be conductive to the continuous release and migration of certain active substances and promotes the localized corrosion; For the particles of size range within 30-75 μm, and the ash deposit amount of 20 mg/cm2, the hierarchical pore structure of the deposit may be conductive to accelerated corrosion, when the cumulative ash amount increases to 30 mg/cm2, the appropriate gradation of particles of different sizes leads to a decrease in the porosity of the deposits, thereby acting as a corrosion barrier. It follows that the most serious corrosion occurred for particles range within 75-100 μm while the ash deposit amount of 10 mg/cm2, the corrosion degree is the next for particles range within 30-75 μm while the ash deposit amount of 20 mg/cm2, in contrast, the corrosion degree was also the most significant when the particle size below 30 μm while the ash deposit amount of 20 mg/cm2. The findings can provide a reference for understanding the characteristics and mechanisms of high-temperature corrosion of boiler tubes in biomass power plants induced by of different sized biomass fly ash.

Key words: alkali metal corrosion    ash corrosion    particle size    ash content    corrosive burst pipe
收稿日期: 2025-09-26      32134.14.1005.4537.2025.304
ZTFLH:  TM621.2  
基金资助:国家自然科学基金(52474214)
通讯作者: 姚锡文,E-mail:yaoxiwen@mail.neu.edu.cn,研究方向为生物质能安全、系统安全理论与技术、工业防火防爆等
Corresponding author: YAO Xiwen, E-mail: yaoxiwen@mail.neu.edu.cn
作者简介: 吴 健,男,2001年生,硕士生
图1  550 ℃燃烧后不同粒度的木屑灰宏观形貌
ElementMass fractionFrame of reference
C0.090.08-0.15
Si0.190.17-0.37
Mn0.420.40-0.70
P0.008≤ 0.25
S0.007≤ 0.010
Cr0.990.90-1.20
Mo0.270.25-0.35
V0.160.15-0.30
表1  12Cr1MoVG化学成分分析结果 (mass fraction / %)
图2  实验系统示意图
图3  不同灰颗粒粒度的XRD谱
图4  粒度< 30 μm下不同涂灰量腐蚀增重曲线
图5  粒度< 30 μm下腐蚀产物表面微观形貌和元素组成分析
图6  粒度< 30 μm的灰颗粒腐蚀示意图
图7  粒度30~75 μm下不同涂灰量腐蚀增重曲线
图8  粒度30~75 μm下腐蚀产物表面微观形貌和元素组成分析
图9  粒度75~100 μm下不同涂灰量腐蚀增重曲线
图10  粒度75~100 μm下腐蚀产物表面微观形貌和元素组成分析
图11  低涂灰量下的腐蚀介质作用示意图
Particle size / μmQuantity of grey applied / mg·cm-2Fitting associative equation (y = axb )aR2
UnplasteredUnplasteredy = 1.4284x0.69411.42840.9842
< 3010y = 1.3115x0.74191.31150.9967
< 3020y = 1.4559x0.73411.45590.9955
< 3030y = 1.1640x0.72541.16400.9842
30-7510y = 1.3417x0.74431.34170.9927
30-7520y = 1.6417x0.69771.64170.9934
30-7530y = 1.2486x0.69751.24860.9883
75-10010y = 1.3757x0.75521.37570.9891
75-10020y = 1.5777x0.68531.57770.9897
75-10030y = 1.4735x0.63401.47350.9820
表2  粒度结合涂灰量的腐蚀增重量拟合关联式
图12  涂灰量10 mg/cm2下不同粒度腐蚀增重曲线
图13  涂灰量20 mg/cm2下不同粒度腐蚀增重曲线
图14  涂灰量30 mg/cm2下不同粒度腐蚀增重曲线
图15  粒度30~75 μm下不同涂灰量下的腐蚀情况
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