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Role of Temperature in Na 2 SO 4 –K 2 SO 4 Deposit Induced Type II Hot Corrosion of NiAl Coating on a Commercial Ni‐Based Superalloy
Author(s) -
Wang Yaping,
Pillai Rishi,
Yazhenskikh Elena,
Frommherz Martin,
Müller Michael,
Naumenko Dmitry
Publication year - 2020
Publication title -
advanced engineering materials
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.938
H-Index - 114
eISSN - 1527-2648
pISSN - 1438-1656
DOI - 10.1002/adem.201901244
Subject(s) - superalloy , nial , materials science , corrosion , coating , oxide , molten salt , metallurgy , phase (matter) , partial pressure , salt (chemistry) , non blocking i/o , microstructure , intermetallic , composite material , catalysis , chemistry , alloy , oxygen , biochemistry , organic chemistry
The life span of gas turbine coatings may be restricted by type II hot corrosion when exposed at elevated temperatures in aggressive environments during service. Herein, the temperature dependence of corrosion morphologies and kinetics of NiAl coating on a second‐generation single crystalline Ni‐based superalloy is studied to provide an insight into the possible corrosion mechanisms. A series of tests are performed at 600–800 °C in air‐300 ppm SO 2 atmosphere with Na 2 SO 4 –20% K 2 SO 4 salt mixture as deposit. Severe attack is observed at both 700 and 750 °C after 24 h exposure, whereas at 600 and 800 °C, only a minor attack is found. The results indicate that the corrosion rate is strongly governed by Na 2 SO 4 –NiSO 4 liquid formation, and temperature affects the attack rate of the outer coating (mainly β‐NiAl phase) primarily by changing the required minimum SO 3 partial pressure to stabilize this liquid. The influence of temperature andp SO 3on phase equilibrium of the salt and oxide mixture is calculated with an in‐house developed thermodynamic database. The predicted minimump SO 3for liquid formation calculated with the database is consistent with the experimental results.