中国腐蚀与防护学报, 2023, 43(4): 890-895 DOI: 10.11902/1005.4537.2022.373

研究报告

20钢及其搪瓷涂层在400 ℃下的氧化和NaCl腐蚀行为研究

袁磊1, 谢新2, 陈明辉,1, 李烽杰1, 王福会1

1.东北大学 沈阳材料科学国家研究中心联合研究分部 沈阳 110819

2.上海船舶工艺研究所 (中国船舶集团有限公司第十一研究所) 上海 200032

Air Oxidation and NaCl Corrosion Behavior of 20 Steel Without and with Enamel Coating at 400 °C

YUAN Lei1, XIE Xin2, CHEN Minghui,1, LI Fengjie1, WANG Fuhui1

1.Shenyang National Key Laboratory for Materials Science, Northeastern University, Shenyang 110819, China

2.Shipbuilding Technology Research Institute (The 11th Institute of China State Shipbuilding Corporation), Shanghai 200032, China

通讯作者: 陈明辉,E-mail:mhchen@mail.neu.edu.cn,研究方向为高温涂层、防腐自润滑

收稿日期: 2022-11-29   修回日期: 2022-12-23  

Corresponding authors: CHEN Minghui, E-mail:mhchen@mail.neu.edu.cn

Received: 2022-11-29   Revised: 2022-12-23  

作者简介 About authors

袁磊,男,1997年生,硕士生

摘要

设计了一种用于20钢表面的搪瓷涂层,研究了基体与搪瓷涂层在400 ℃下恒温氧化1000 h和表面涂覆氯盐200 h的腐蚀行为。结果表明,搪瓷涂层呈非晶态,致密平整,与基体结合良好。在长时间的实验中未出现开裂或剥落行为,具有很高的热稳定性以及耐蚀性,为20钢基体提供了有效的防护。

关键词: 搪瓷涂层 ; 20钢 ; 恒温氧化 ; 氯盐腐蚀

Abstract

A novel enamel coating was prepared on 20 steel, then the oxidation and NaCl deposit induced corrosion of the steel without and with enamel coating were studied in air at 400 ℃ for 1000 and 200 h respectively. It is revealed that the prepared enamel coating is compact, amorphous, and can be well combined with the substrate. There are no cracks and spallation of enamel coatings was observed after corrosion tests. The enamel coating has high thermal stability and corrosion resistance, which provides effective protection for the 20 steel substrate.

Keywords: enamel coating ; 20 steel ; oxidation ; chlorine salt corrosion

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袁磊, 谢新, 陈明辉, 李烽杰, 王福会. 20钢及其搪瓷涂层在400 ℃下的氧化和NaCl腐蚀行为研究. 中国腐蚀与防护学报[J], 2023, 43(4): 890-895 DOI:10.11902/1005.4537.2022.373

YUAN Lei, XIE Xin, CHEN Minghui, LI Fengjie, WANG Fuhui. Air Oxidation and NaCl Corrosion Behavior of 20 Steel Without and with Enamel Coating at 400 °C. Journal of Chinese Society for Corrosion and Protection[J], 2023, 43(4): 890-895 DOI:10.11902/1005.4537.2022.373

随着人口的不断增长和城市化率的提高,城市固体废物的产生量也迅速增加,垃圾已成为社会上的热点和难点问题。近年来,垃圾焚烧技术因减容率高,可发电、节约土地资源等诸多优点而越来越受到重视[1~3]。城市垃圾如废塑料、橡胶等在高温焚烧后会生成NaCl、KCl等大量腐蚀性物质,焚烧锅炉零部件如过热器、水冷壁等会被这些物质腐蚀变薄甚至爆裂[4,5]。为了降低电厂的运营成本和安全风险,通常将锅炉温度和压力限制在400 ℃和4 MPa以内[6,7]

我国常用的锅炉用钢为20G钢[7],但这种低成本钢通常不能抵抗实际腐蚀环境,因此,在其上涂覆耐蚀涂层是常用做法。目前主要采用表面堆焊[8]、喷涂[9]其他耐蚀合金方法,但这种金属类涂层在长期服役过程中也会与腐蚀介质发生反应从而出现涂层退化问题,同时这也会使得原材料成本大幅上升。近年来,有机与无机非金属涂层因原料便宜,耐蚀性高等优点而受到研究者越来越多的关注,传统有机涂层可解决常温下盐雾腐蚀问题,但高温下清漆易发生严重的热分解导致涂层失效[10,11]。搪瓷涂层作为无机非金属氧化物的复合体,服役时不存在类似金属类涂层的退化问题,具有高热化学稳定性[12]。目前对于搪瓷涂层的研究主要集中在高温领域的发动机叶片[13,14]、燃气轮机[15,16],以及常温领域的石油管道[17]、锅炉热交换器 (GGH)[18]、生物活性玻璃等[19,20],而在中温领域的研究为数不多。针对于此,本文选取与20G成分相似的20钢为基体,探索在其上施加搪瓷涂层的可行性,并试验了涂层在400 ℃下恒温氧化以及氯盐加速腐蚀环境中的防护能力表现。

1 实验方法

20钢的化学成分 (质量分数,%) 为:C 0.17~0.23, Si 017~0.37, Mn 0.35~0.65, P≤0.035, S≤0.035, Ni≤0.3, Cr≤0.25, Fe为余量。其碳含量为0.2%左右,而搪瓷用钢碳含量一般不超过0.1%[21]。碳含量过高会使得搪烧过程中产生大量气泡,造成搪瓷表面发泡、开裂等缺陷。针对这个问题可以适当提高Na2O、K2O等助溶剂含量来解决,同时加入Al2O3等原料兼顾耐蚀性[22]。详细瓷釉配方 (质量分数,%) 为:SiO2 52,B2O3 12, Al2O3 6,K2O 5.5,Na2O 11,CaF2 6,Li2O 6,CoO 1.5。经前期探索,该涂层最佳烧结工艺为:780 ℃下烧结2 min。

将上述原料装入氧化铝坩埚并加热至1300 ℃形成熔融玻璃,水淬和研磨后得到搪瓷粉末。将基体切割成15 mm×10 mm×2.5 mm大小的试样,并使用SiC砂纸研磨至1000粒度。首先对基体进行喷砂处理,然后在丙酮中进行超声波清洗,将混合有乙醇的搪瓷粉末利用空气压缩机喷涂到试样的粗糙表面上,然后在100 °C下干燥5 min,在780 ℃马弗炉里烧结2 min以形成搪瓷涂层。

氧化在马弗炉里进行,经称重和测量表面积后,将样品放在预先烧至恒重的刚玉坩埚中,在实验温度下的静止空气中氧化,间隔一定时间取出,空冷至室温,在精度为10-5 g的电子天平上称重得到动力学曲线,然后放入炉中继续氧化。实验温度为400 ℃,氧化时间为1000 h。为了得到氧化规律,前期取样频次适当增多,后500 h每隔100 h取一次。

氯盐腐蚀实验在马弗炉中进行,选用饱和NaCl溶液。首先将饱和盐溶液均匀地涂在预热的试样表面,涂盐量为1.5~2.5 mg/cm2,然后将试样置于400 ℃的马弗炉内保温一定时间后取出,空冷至室温后置于沸腾的去离子水中洗去残留盐,最后烘干、称重,以此作为一个循环。为减小误差,每组样品准备了3个平行样,用精度为10-5 g的电子天平记录样品的重量变化。

使用Inspect F50扫描电子显微镜 (SEM) 并结合X-Max能谱仪 (EDS) 分析涂层形貌及成分,利用X'Pert PRO X射线衍射仪 (XRD) 分析相组成 (Cu ,40 kV)。

2 结果与讨论

2.1 搪瓷涂层制备态微观形貌

图1显示了制备态搪瓷涂层表面、截面形貌以及XRD谱。从图中可看出,涂层表面十分致密平整,且与基体结合良好,截面涂层中出现大小不一的气泡是由于瓷釉熔体在冷却时粘度较大,产生的CO、CO2等气体来不及迁移而残留于涂层内部,形成闭口气孔,这是典型的搪瓷涂层微观形貌[23]图1c显示搪瓷呈粉末状时为玻璃非晶态,在25°附近出现一个典型的非晶馒头峰。作为涂层时检测到的唯一晶相是Fe,与基体峰相同,这是由于搪瓷涂层本质为微晶玻璃,当涂层中无其他相析出时,X射线能穿透玻璃到达基体表面从而检测出基体相[24]

图1

图1   制备态搪瓷涂层的表面和截面形貌以及XRD谱

Fig.1   Surface (a) and cross-sectional (b) morphologies and XRD spectra (c) of as-prepared enamel coating on 20 steel


2.2 400 ℃恒温氧化

图2为带涂层和不带涂层的20钢在400 ℃下氧化1000 h后的动力学曲线。从中可看出,施加搪瓷涂层后明显降低了20钢的氧化速率。对于20钢基体,氧化1000 h后,增重达到了0.64 mg/cm2,而带涂层的样品增重仅0.02 mg/cm2,几乎不增重。裸钢的氧化动力学曲线前期遵循抛物线规律,后期氧化速度则有所放缓,而带有涂层的样品则近似处于一条水平直线上。

图2

图2   不带及带有搪瓷涂层的20钢在400 ℃下的氧化动力学曲线

Fig.2   Oxidation kinetics of 20 steel with and without enamel coating at 400 ℃


图3显示了氧化不同时间后的基体截面照片,可看出氧化10 h后表面形成较薄的氧化膜,且与基体之间存在裂隙,说明氧化膜未完全铺展在基体表面。100 h后便形成较为致密的氧化膜,表明前期氧化速度较快,根据动力学曲线也可得知前100 h氧化膜完全按抛物线规律增长。100 h后氧化膜厚度增长放缓,EDS以及XRD分析得知氧化膜成分主要为Fe3O4图3a表层晶须状物质对应为针尖状的Fe2O3,如图所示,这是铁基金属氧化特点,即Fe2O3以晶须状在Fe3O4上生长[25]。从图3cd可看出氧化膜间出现了裂缝,并且随氧化时间越长越明显。

图3

图3   20钢基体氧化不同时间后背散射扫描像

Fig.3   Cross-sectional BSE-mode images of the bare 20 steel after oxidation at 400 ℃ for 10 h (a), 100 h (b), 500 h (c) and 1000 h (d). The inset in Fig.3a shows the surface morphology


图4为搪瓷涂层氧化1000 h后表面以及截面照片,表面出现许多颗粒状玻璃微粒,猜测为搪瓷涂层长期氧化后表面出现一层脆性凝胶状物质,在重复取样过程中反复受急冷,应力集中来不及释放导致凝胶层破碎,然而从截面上看涂层仍均匀致密,未遭到破坏,表明凝胶层极薄,对整个涂层几乎无影响。图4c为横截面Si、O等主要元素的线扫结果,可看出O在整个横截面分布均匀,涂层/基体界面处并无明显增加,这表明搪瓷涂层具有优异的阻氧能力。

图4

图4   400 ℃下氧化1000 h后搪瓷涂层微观表征

Fig.4   Surface (a), cross section (b) and corresponding EDS line scannings (c) for the enamel coating oxidized at 400 °C for 1000 h


有报道在硅酸盐玻璃的阻氧扩散方面,氧的扩散是通过溶解的氧分子与网络中的氧之间的交换来进行的[26,27],搪瓷是由多种氧化物通过熔炼-冷淬方式形成的脆性非晶材料,其独特的网状结构能有效阻止腐蚀气氛的向内扩散以及合金元素的向外扩散。在本实验温度下,氧在搪瓷内部的扩散系数极低,同时,配方原料中加入的少量氧化铝可以Al-O四面体基团溶入Si-O网络中[22],增强搪瓷的网络结构以及提高搪瓷的黏度,延长氧的交换过程,从而提高了阻氧扩散能力。

2.3 400 ℃氯盐腐蚀

动力学曲线是腐蚀产物生成与剥落的综合结果。从图5看出,基体的增重曲线在初期波动很大,结合扫描照片可知此时便已发生较为严重的腐蚀,表面已形成较厚腐蚀膜,从图6a可知基体已经开始出现剥落趋势。腐蚀10 h便开始出现失重现象,表明腐蚀产物剥落量大于产生量,从图6bd腐蚀200 h后的扫描照片来看,基体表面已经遭受了严重的破坏,形成分散破裂的腐蚀膜,从截面也可看出腐蚀膜呈多层相互分离状,XRD结果表明腐蚀膜主要成分为Fe3O4,表面晶须状为Fe2O3。表面分散的多层腐蚀膜也表明基体受到了反复的氯盐腐蚀,这也解释了动力学曲线上先失重后增重现象。而带有搪瓷涂层的样品动力学曲线一直很平稳,腐蚀200 h后的扫描结果如图7所示,可看出涂层腐蚀后仍旧致密平整,未遭到破坏。从图7c中XRD结果可知搪瓷涂层在整个腐蚀期间并未生成其他相,表明涂层能稳定存在于氯盐环境中,表现出优异的耐蚀性能。

图5

图5   不带及带有搪瓷涂层的20钢在400 oC下表面沉积NaCl时增重曲线

Fig.5   Mass changes of 20 steel without and with enamel coating at 400 ℃ under the condition of NaCl deposition


图6

图6   20钢表面沉积NaCl时400 °C下腐蚀后的形貌

Fig.6   Surface morphologies (a, b) and cross sections (c, d) of 20 steel after NaCl pre-deposited corrosion at 400 °C for 5 h (a, c) and 200 h (b, d)


图7

图7   带搪瓷涂层的20钢在表面沉积NaCl时腐蚀200 h后微观表征

Fig.7   Surface (a), cross section (b) and XRD pattern (c) of enamel coating after NaCl pre-deposited corrosion at 400 ℃ for 200 h


氯盐腐蚀属于工业上常见的腐蚀类型,在实验温度下,NaCl可直接与金属发生反应:

2NaCl+5O2+6Fe=2Fe2O3+
Na2Fe2O4+Cl2     (ΔG=-1715.7 kJ/mol)

释放出Cl2。通常氯在氧化膜中有很强的渗透性,能够穿过氧化膜到达氧化膜/金属界面与金属反应:

Fe+Cl2=FeCl2     (ΔG=-255.4 kJ/mol)

生成挥发性氯化物FeCl2,FeCl2在向外扩散过程中又会发生如下氧化反应:

FeCl2+3/4O2=1/2Fe2O3+Cl2
(ΔG=-65.5 kJ/mol)

生成的Fe2O3与无氯环境下氧化膜相比黏附性差,疏松多孔,极大破坏了原有氧化膜的致密性,最终导致氧化膜更严重的开裂与脱落,部分生成的Cl2又会回到氧化膜/金属界面重复上述腐蚀过程,直至氯被耗尽为止,这个过程称为氯的“活化氧化”[28]。搪瓷涂层本质为惰性氧化物的结合体,在氧化和热腐蚀过程中本身不会继续被氧化,其连续致密的微观网络结构能在保持较高热稳定性的同时可以显著地抑制外界环境中Cl-等腐蚀介质向基体中的扩散。搪瓷涂层的防护机制主要为惰性氧化物的物理阻隔作用。

3 结论

20钢基体在400 ℃长期恒温氧化以及氯盐腐蚀环境中均表现出较差的耐蚀性,氯盐腐蚀尤为严重,初期便已失去抵御能力。

搪瓷涂层在两种环境下均表现出极高的热稳定性与极低的腐蚀速率,涂层在实验过程中保持完整致密,有效地阻挡了O、Cl等腐蚀介质向涂层/基体界面扩散,在盐膜与合金基体之间保持长期稳定的阻隔作用,极大地提高了20钢在氯盐环境中的耐蚀能力。搪瓷涂层的耐腐蚀机制主要为物理阻隔作用。

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The aim of this work is to identify the current level of energy recovery through waste thermal treatment. The state of the art in energy recovery from waste was investigated, highlighting the differences for different types of thermal treatment, considering combustion/incineration, gasification and pyrolysis. Also different types of wastes - Municipal Solid Waste (MSW), Refuse Derived Fuel (RDF) or Solid Refuse Fuels (SRF) and some typologies of Industrial Waste (IW) (sludge, plastic scraps, etc.) - were included in the analysis. The investigation was carried out mainly reviewing papers, published in scientific journals and conferences, but also considering technical reports, to gather more information. In particular the goal of this review work was to synthesize studies in order to compare the values of energy conversion efficiencies measured or calculated for different types of thermal processes and different types of waste. It emerged that the dominant type of thermal treatment is incineration associated to energy recovery in a steam cycle. When waste gasification is applied, the produced syngas is generally combusted in a boiler to generate steam for energy recovery in a steam cycle. For both the possibilities--incineration or gasification--co-generation is the mean to improve energy recovery, especially for small scale plants. In the case of only electricity production, the achievable values are strongly dependent on the plant size: for large plant size, where advanced technical solutions can be applied and sustained from an economic point of view, net electric efficiency may reach values up to 30-31%. In small-medium plants, net electric efficiency is constrained by scale effect and remains at values around 20-24%. Other types of technical solutions--gasification with syngas use in internally fired devices, pyrolysis and plasma gasification--are less common or studied at pilot or demonstrative scale and, in any case, offer at present similar or lower levels of energy efficiency.Copyright © 2014 Elsevier Ltd. All rights reserved.

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