Abstract
One way of controlling alkali chloride-induced corrosion in biomass boilers is by designing new alloy materials used as superheater tubes. Four newly designed Cr–Ni alloy was designed and studied for applicability in biomass power plants. High-temperature oxidation experiments and high-temperature corrosion experiments were carried out for evaluation material characterization. Through analysis and discussion of the corrosion kinetics and oxidation kinetics, it can be concluded that materials with series number of “2xx” and “3xx” had better endurance ability in KCl environment under 650°C and 700°C than TP316 material. In the same conditions, 3xx material had better anticorrosion ability in 700°C with KCl environment.
Introduction
There exists serious molten salt corrosion for superheater material at high temperature in the flue gas side of biomass boilers due to high concentration of chloride salts in biomass fuels [1]. Alkali chlorides are aggressive and can react with the steel surface at high temperature, which may enhance local oxidation. It has been shown that high-temperature corrosion of stainless steels is greatly enhanced by the presence of KCl, especially for large power capacity of biomass power plant [2–4].
In order to acquire cost-effective performance of material, newly designed material is a possible way to explore alternative selection for superheater tubes. Because austenite steel has special advantages in chloride environment, new materials were designed by adjustment of chromium–nickel concentration in alloy. This article has designed and analyzed several kinds of new Cr–Ni stainless steel with relative appropriate cost. According to corrosion analysis and discussion, anticorrosion lifetime prediction and performance comparison were also conducted.
Experiment
Material design
Because austenite stainless steel has good performance for its face-centered cubic of austenite structure [5–7], Cr–Ni series steel has been taken into account for new materials. In order to strengthen anticorrosion performance, chromium was mainly considered by improving its concentration. At the same time, austenite structure was also a must. Table 1 lists chemical compositions of newly designed material. In the column of “sample series,” “1xx” indicates the first kind of Cr–Ni materials, and “4xx” means the fourth kind of Cr–Ni materials. These four materials were manufactured by smelting method. TP316 is used as a reference sample for performance comparison of material.
Chemical compositions of newly designed materials.
N° | Sample series | WC, % | WCr, % | WNi, % | WFe, % |
1 | 1xx | 0.05 | 25.2 | 1.0 | Rest |
2 | 2xx | 0.05 | 23.2 | 3.0 | Rest |
3 | 3xx | 0.05 | 21.2 | 5.0 | Rest |
4 | 4xx | 0.05 | 20.2 | 6.0 | Rest |
5 | TP316 | 0.03 | 17.0 | 12.0 | Rest |
Samples and arrangement
Material samples were fabricated into sheet specimens of 50 × 25 × 2 mm. The surface of each sample was treated in turn by the metallurgical sandpaper, ethanol and acetone solution. Then each sample was treated with the sandpaper and placed in a drying box at 150°C for 2 h. Weighing and measuring the length/width and thickness, microstructure characterization was carried out before the experiment.
Material samples were placed in a box-type resistance furnace for testing. With the help of a fine ceramic tube, as shown in Figure 1, metal samples were suspended in the top of the alumina crucible with size of Φ200 × 150 mm. Before the start of each experiment, KCl electrolyte was put in the bottom of the crucible and can form a certain thickness of the salt bed. When samples were heated to high temperature, solid KCl was heated and transformed into KCl vapor. The former samples would only endure KCl vapor. The latter samples would endure both KCl vapors and high-temperature KCl electrolyte.

Schematic view for sample arrangement of high-temperature corrosion experiment.Note: 1, crucible; 2, crucible groove; 3, suspended sample; 4, fine ceramic tube; 5, KCl.
Corrosion experiments
The experimental temperatures were set at 600°C, 650°C and 700°C. In accordance with “simple static oxidation test” [8], weight method was used for evaluation of high-temperature corrosion kinetics. The exposure time was set to 30 h. During experimental process, samples would be taken out in different times, such as 1, 4, 7, 10, 20 and 30 h. Each sample would be checked and measured for observation of their morphology change and massive change. The corrosion kinetic curves and oxidation kinetic curves can be drawn according to weight changes data from experimental time. Different material would present completely different kinetic law. During the analytical process, Origin 9.0 and Matlab 2013b were employed for data analysis and modeling.
Experimental results
High-temperature experiments for different material
Figure 2 shows weight changes during the corrosion process in KCl for four test materials and reference TP316 material in 600°C. It can be seen there was a small quantity of weight increase for all materials. During the first 15 h, TP316 had higher corrosion increases than other materials. In the final experimental stage, the largest corrosion increase was not higher than 1.5 mg/cm2. Figure 3 shows weight changes during the corrosion process in KCl for four test materials and reference TP316 material in 650°C. TP316 showed negative weight change during the corrosion process, which indicated that layer materials have poor adhesion property in the surface of the material matrix due to spalled oxide flakes found in the furnace after the exposure. Tested material, from 1xx to 4xx, showed relatively low weight increase. The largest corrosion increase was no higher than 4.0 mg/cm2.

Weight changes during the corrosion process in KCl for four test materials and reference TP316 at 600°C.

Weight changes during the corrosion process in KCl for four test materials and reference TP316 at 650°C.
Figure 4 shows weight changes during the corrosion process in KCl for four test materials and reference TP316 material in 700°C. It can be seen that 4xx material cannot endure such condition and showed obvious negative weight change during the corrosion process. The tendency was even worse than that of TP316 material. In the final experimental stage, 3xx material showed the tendency of the weight decrease. The quality of the layer on the surface of 3xx material was inferior to 2xx, 1xx material. Figure 5 shows weight changes of high-temperature oxidation processes in air environment for four test materials and reference TP316 material in 700°C. We can see that TP316 and 1xx material showed relatively higher weight increase during the corrosion process. The largest value of the weight increase was not higher than 0.35 mg/cm2, which showed that the oxidation process was relatively stable and the oxidation layer was of denser materials with possible protective ability. All materials have no phenomenon of negative weight change, which displayed that the oxidation layer was in a good state, especially in condition of 700°C.

Weight changes during the corrosion process in KCl for four test materials and reference TP316 at 700°C.

Weight changes for four test materials and reference TP316 at 700°C in air.
Experimental results in different temperatures
Because 4xx presented inferior anticorrosion ability in Figure 4 and 1xx presented inferior antioxidation ability in Figure 5, 2xx and 3xx materials were mainly analyzed in different temperatures. Figure 6 shows weight changes of 2xx material in different temperatures. Except 700°C air conditions, other experiments were all in KCl medium condition. We can note that the high-temperature oxidation process displayed the smallest corrosion increase. In KCl condition, with increase of temperature, the corrosion increase increased quickly and obviously. Figure 7 shows weight changes of 3xx material in different temperatures. Except 700°C air conditions, other experiments were all in KCl medium condition. We can see that the tendency of 3xx material was similar to that of 2xx material. In 650°C KCl conditions, 3xx materials displayed highest weight increase in all four experiments. In 700°C KCl conditions, there was the appearance of negative weight change, which may result in nonprotective layer with poor adhesion property to the material surface.

Weight changes during the corrosion process in different temperatures for 2xx material.

Weight changes during the corrosion process in different temperatures for 3xx material.
Analysis and discussion
Comparison analyses of anticorrosion ability
According to Figure 2, in 600°C conditions with saturated KCl environment, TP316 showed longer anticorrosion lifetime in relatively low temperature condition. However, Figures 3 and 4 indicate that TP316 presented the obvious disadvantages to 650°C and 700°C conditions. In comparison, 2xx and 3xx materials had better oxide layer on the surface of tested samples in such conditions because of relatively lower weight changes during corrosion process.
Table 2 displays analytic data of correlation coefficient for five materials in 700°C, KCl condition. Spearman correlation analysis was employed due to non-normal distribution data of the corrosion process. It can be seen that 1xx and 4xx materials had very high negative correlation with r=−0.96429. There was also a high correlation between 2xx and 3xx materials with r=0.92857. TP316 had great similarity in anticorrosion performance with 1xx and 4xx materials, while it had no correlation with 2xx and 3xx materials.
Spearman correlation analysis for five materials in 700°C, KCl condition.
1xx | 2xx | 3xx | 4xx | |
2xx | r=−0.42857 | / | ||
p=0.33737 | ||||
3xx | r=−0.64286 | r=0.92857 | / | |
p=0.11939 | p=0.00252 | |||
4xx | r=−0.96429 | r=0.57143 | r=0.78571 | / |
p=0.00045 | p=0.1802 | p=0.03624 | ||
TP316 | r=−1 | r=0.08571 | r=0.42857 | r=0.94286 |
– | p=0.87174 | p =0.3965 | p =0.0048 |
Note: The higher the value of r was, the similar the performance between two materials was. If the value of r was minus, it indicated that the performance between two materials was completely on the contrary.
Fitting function models of corrosion kinetic processes for four newly designed materials
Table 3 shows the comparison of fitting function of five different materials in 700°C, KCl condition. Much corrosion data were treated with Matlab 2013b. Fitting accuracy was not allowed to be less than 0.99 for R2 of fitting function. Based on these fitting functions, weight increase quantity can be predicted for longer corrosion time, such as 50 h. Table 3 indicates that predicted values for 50 h were relatively better for 3xx material.
Comparison analysis of fitting function for five different materials.
Fitting type | Degree | Sum of squares of error (SSE) | R2 | Weight increase quantity for 50 h | |
1xx | Polynomial | 5 | 0.001092 | 0.9994 | −24.156 |
2xx | Polynomial | 4 | 0.06196 | 0.9906 | −110.82 |
3xx | Polynomial | 5 | 0.004226 | 0.9994 | 680.2 |
4xx | Polynomial | 5 | 0.02051 | 0.9999 | 3,090 |
TP316 | Polynomial | 6 | 5.486e-23 | 1 | 23,473 |
Anticorrosion lifetime predictions of newly designed materials in biomass power plant
Table 4 shows the comparison of fitting function of three temperatures for 3xx material in KCl condition. According to these fitting functions, anticorrosion lifetimes can be estimated for a special weight increase of 50 mg/cm2. Table 4 indicates that 3xx material can endure 37.6 h in 700°C KCl conditions when weight increase is 50 mg/cm2. However, TP316 and 4xx materials displayed very early spalling according to Figure 4.
Comparison analysis of fitting function for 3xx material in different temperatures.
Fitting type | Degree | SSE | R2 | Lifetime for 50 mg/cm2 | |
600°C | Polynomial | 1 | 0.004159 | 0.9939 | 1,500 h |
650°C | Polynomial | 5 | 0.003003 | 0.9984 | 39.6 h |
700°C | Polynomial | 5 | 0.004226 | 0.9994 | 37.6 h |
Conclusions
In comparison, 2xx and 3xx materials had better endurance ability in 650°C and 700°C KCl condition than TP316 materials. TP316 had great similarity in anticorrosion performance with 1xx and 4xx materials, while it had no correlation with 2xx and 3xx materials. There was a high correlation between 2xx and 3xx materials with r=0.92857. In the same conditions, 3xx material had better anticorrosion ability for its predicted values for 50 h in 700°C with KCl environment. The predicted anticorrosion lifetime for 3xx material is 37.6 h of 700°C KCl conditions when weight increase is 50 mg/cm2, which is far superior to other materials in such condition.
Acknowledgments
This work was sponsored by the Electric Power Research Institute of Guangdong Power Grid Co., Ltd. The authors are grateful to all reviewers of the manuscript for their encouraging comments.
References
[1] S. Enestam, D. Bankiewicz, J. Tuiremo et al., Fuel, 104 (2013) 294–306.10.1016/j.fuel.2012.07.020Search in Google Scholar
[2] R.A. Antunes and M.C. Oliveira, Corros. Sci., 76 (2013) 6–26.10.1016/j.corsci.2013.07.013Search in Google Scholar
[3] H. Kassman, J. Pettersson, B.M. Steenari et al., Fuel Process. Technol., 105 (2013) 170–180.10.1016/j.fuproc.2011.06.025Search in Google Scholar
[4] H.B. Li, Z.H. Jiang, Y. Yang et al, Int. J. Miner. Metall. Mater., 16 (2009) 517–524.10.1016/S1674-4799(09)60090-XSearch in Google Scholar
[5] A. Valor and F. Caleyo, Corros. Sci., 49 (2007) 559–579.10.1016/j.corsci.2006.05.049Search in Google Scholar
[6] J. Yin, Z. Wu and J. Chin, Chem. Eng., 17 (2009) 849–853.Search in Google Scholar
[7] J. Lehmusto, P. Yrjas, B.J. Skrifvars et al, Fuel Process. Technol., 104 (2012) 253–264.10.1016/j.fuproc.2012.05.020Search in Google Scholar
[8]W. Luo, Z. Liu, Y.T. Wang et al., Procedia Eng., 36 (2012) 212–216.10.1016/j.proeng.2012.03.033Search in Google Scholar
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Articles in the same Issue
- Frontmatter
- Short Communication
- Microscale Interface Synthesis of Ni-B Amorphous Nanoparticles from NiSO4 by Sodium Borohydride Reduction in Microreactor
- Research Articles
- The Effect of Post-heat Treatment on the Microstructures of Single Crystal DD6 Superalloy
- Changes in the Material Properties of Steel 1.4762 Depending on the Temperature
- Formation of Ti5Si3 by Combustion Synthesis in a Self-Propagating Mode: Experimental Study and Numerical Simulation
- Effect of Processing Parameters on Plasma Jet and In-flight Particles Characters in Supersonic Plasma Spraying
- Crystallization Behavior and Growing Process of Rutile Crystals in Ti-Bearing Blast Furnace Slag
- Evaluation of Anticorrosion Performance of New Materials for Alternative Superheater Tubes in Biomass Power Plants
- Investigation on Burden Particle Softening and Melting Process under High Reduction Potential Condition
- Application of response surface methodology for optimization of parameters for microwave heating of rare earth carbonates
- Interfacial Evolution of Cement and Steel in CO2 Dissolved Solution Under High Temperature and High Pressure
- Study of Dissolution Process of Solid Cu in Liquid Al
- The Pin-Loaded Small One-Bar Specimen in Use to Determine Uniaxial and Multiaxial Creep Data
- Vertical Compensation Friction Stir Welding of 6061-T6 Aluminum Alloy