Critical Crevice (CCT) and Critical Pitting (CPT) Temperatures in Acidified Ferric Chloride (ASTM G 48, Methods D and C) |
To assess the resistance of alloys to pitting and crevice attack, it is customary to measure their Critial Crevice Temperatures and Critical Pitting Temperatures in acidified 6 wt.% ferric chloride, in accordance with the procedures defined in ASTM Standard G 48. These values represent the lowest temperatures at which crevice attack and pitting attack are encountered in acidified ferric chloride, within 72 hours.
| |
Critical Crevice Temperatures |
Critical Pitting Temperatures |
| ALLOY |
°C |
°F |
°C |
°F |
| 316L |
0 |
32 |
15 |
59 |
| 254SMO® |
30 |
86 |
60 |
140 |
| 625 |
40 |
104 |
100 |
212 |
| C-22 |
80 |
176 |
>120 |
>248 |
| C-276 |
55 |
131 |
>120 |
>248 |
| C-2000 |
80 |
176 |
>120 |
>248 |
|
| Critical Pitting Temperatures in Green Death Solution |
Another solution commonly used for assessing the pitting resistance of nickel alloys is 11.5% sulfuric acid + 1.2% hydrochloric acid + 1% ferric chloride + 1% cupric chloride, otherwise known as Green Death. Listed are Critical Pitting Temperatures of C-2000 and other alloys in Green Death, based on tests of 24 hours.
| |
Critical Crevice Temperatures |
| ALLOY |
°C |
°F |
| 316L |
25 |
77 |
| 625 |
75 |
167 |
| C-4 |
90 |
194 |
| C-22 |
120 |
248 |
| C-276 |
105 |
221 |
| C-2000 |
110 |
230 |
|
| Seawater Crevice Corrosion Results |
Seawater is probably the most common aqueous salt solution. Not only is it encountered in marine transportation and offshore oil rigs, but it is also used as a coolant in coastal industries. Listed are some recent data, generated as part of a U.S. Navy study at the LaQue Laboratories in Wrightsville Beach, North Carolina.* Crevice tests were performed in both still (quiescent) and flowing seawater, at 29°C, plus or minus 3°C. Two samples of each alloy were tested in still water for 180 days, and two samples of each alloy were tested in flowing water for 180 days. Each sample contained two possible crevice sites.
| |
Quiescent |
Quiescent |
Flowing |
Flowing |
| ALLOY |
No. of Sites |
Depth, mm |
No. of Sites |
Depth, mm |
| 316L |
2 |
1.80 |
2 |
0.32 |
| 254SMO |
2 |
1.25 |
2 |
0.01 |
| 625 |
2 |
0.11 |
2 |
<0.01 |
| C-22 |
0 |
0 |
0 |
0 |
| C-276 |
1 |
0.12 |
0 |
0 |
| C-2000 |
0 |
0 |
0 |
0 |
*Ref. D. M. Aylor et al, Paper No. 329, CORROSION 99, NACE International, 1999. |
| Uniform Corrosion Data (C-2000, C-4, C-22, C-276, 625) |
| Chemical |
Conc. |
Temperature |
Corrosion Rate |
| wt.% |
°C |
°F |
C-2000 |
C-4 |
C-22 |
C-276 |
C-625 |
mm/y |
mpy |
mm/y |
mpy |
mm/y |
mpy |
mm/y |
mpy |
mm/y |
mpy |
| Hydrochloric Acid |
1 |
Boiling |
0.01 |
0.2 |
0.48 |
18.8 |
0.06 |
2.2 |
0.33 |
13.0 |
0.23 |
8.9 |
| 5 |
79 |
175 |
<0.01 |
0.1 |
0.98 |
38.6 |
1.44 |
56.6 |
0.75 |
29.4 |
4.65 |
183.0 |
| 10 |
38 |
100 |
<0.01 |
<0.1 |
0.19 |
7.3 |
0.01 |
0.4 |
0.17 |
6.8 |
0.30 |
11.9 |
| 20 |
38 |
100 |
0.16 |
6.3 |
0.14 |
5.4 |
0.20 |
7.7 |
0.14 |
5.4 |
0.36 |
14.1 |
| Hydrobromic Acid |
2.5 |
Boiling |
0.01 |
0.2 |
0.08 |
3.3 |
0.02 |
0.6 |
0.13 |
5.0 |
<0.01 |
0.1 |
| 5 |
93 |
200 |
0.01 |
0.2 |
0.76 |
29.9 |
0.01 |
0.3 |
0.15 |
5.8 |
0.60 |
23.7 |
| 7.5 |
93 |
200 |
<0.01 |
0.1 |
0.76 |
29.9 |
0.45 |
17.8 |
0.73 |
28.7 |
0.93 |
36.5 |
| 10 |
79 |
175 |
<0.01 |
<0.1 |
0.53 |
20.9 |
0.01 |
0.3 |
0.51 |
20.0 |
0.82 |
32.3 |
| 20 |
66 |
150 |
<0.01 |
<0.1 |
0.35 |
13.7 |
0.46 |
18.2 |
0.37 |
14.5 |
0.65 |
25.7 |
| Hydrofluoric Acid |
1 |
79 |
175 |
0.18 |
7.0 |
N/T |
N/T |
0.21 |
8.2 |
0.40 |
15.9 |
0.31 |
12.2 |
| 5 |
52 |
125 |
0.09 |
3.7 |
N/T |
N/T |
0.15 |
6.0 |
0.34 |
13.4 |
0.70 |
27.4 |
| 10 |
52 |
125 |
0.22 |
8.7 |
N/T |
N/T |
0.33 |
13.1 |
0.41 |
16.0 |
2.23 |
87.8 |
| 20 |
52 |
125 |
0.48 |
18.8 |
N/T |
N/T |
0.53 |
21.0 |
0.48 |
18.8 |
4.33 |
170.5 |
| Sulfuric Acid |
10 |
93 |
200 |
0.02 |
0.8 |
0.19 |
7.3 |
0.04 |
1.6 |
0.14 |
5.5 |
0.24 |
9.5 |
| 20 |
93 |
200 |
0.03 |
1.0 |
0.38 |
15.1 |
0.28 |
11.0 |
0.40 |
15.6 |
0.58 |
23.0 |
| 30 |
93 |
200 |
0.04 |
1.5 |
0.54 |
21.3 |
0.68 |
26.8 |
0.42 |
16.4 |
0.68 |
26.9 |
| 40 |
79 |
175 |
0.01 |
0.5 |
0.38 |
15.0 |
0.31 |
12.3 |
0.19 |
7.5 |
0.58 |
22.8 |
| 50 |
79 |
175 |
0.02 |
0.7 |
0.63 |
24.7 |
0.40 |
15.9 |
0.26 |
10.3 |
0.89 |
35.2 |
| 60 |
79 |
175 |
0.02 |
0.9 |
0.67 |
26.4 |
0.67 |
26.4 |
0.30 |
11.8 |
0.92 |
36.2 |
| 70 |
66 |
150 |
0.01 |
0.2 |
0.14 |
5.7 |
0.28 |
11.0 |
0.05 |
1.8 |
0.63 |
24.7 |
| 80 |
66 |
150 |
0.06 |
2.2 |
0.13 |
5.1 |
N/T |
N/T |
0.04 |
1.6 |
0.91 |
35.8 |
| 90 |
79 |
175 |
0.07 |
2.9 |
0.71 |
27.9 |
N/T |
N/T |
0.05 |
1.9 |
6.97 |
274.5 |
| Nitric Acid |
20 |
Boiling |
0.02 |
0.7 |
0.38 |
15.0 |
0.06 |
2.3 |
0.66 |
25.9 |
0.01 |
0.3 |
| 40 |
Boiling |
0.24 |
9.5 |
1.27 |
50.0 |
0.26 |
10.4 |
4.42 |
174.0 |
0.14 |
5.5 |
| 60 |
93 |
200 |
0.19 |
7.4 |
0.73 |
28.7 |
0.19 |
7.6 |
2.03 |
80.0 |
0.06 |
2.4 |
| 70 |
93 |
200 |
0.29 |
11.4 |
0.95 |
37.4 |
0.33 |
13.0 |
2.62 |
103.0 |
0.08 |
3.2 |
| Phosphoric Acid |
50 |
Boiling |
0.03 |
1.1 |
0.27 |
10.7 |
0.03 |
1.3 |
0.18 |
6.9 |
0.02 |
0.9 |
| 60 |
Boiling |
0.08 |
3.2 |
0.11 |
4.3 |
0.56 |
21.9 |
0.28 |
11.1 |
0.16 |
6.2 |
| 70 |
Boiling |
0.15 |
6.0 |
0.13 |
5.1 |
1.04 |
41.0 |
0.13 |
5.2 |
0.89 |
35.2 |
| 80 |
Boiling |
0.40 |
15.6 |
0.26 |
10.3 |
3.02 |
119.0 |
0.31 |
12.3 |
4.90 |
193.0 |
| Chromic Acid |
10 |
66 |
150 |
0.10 |
3.9 |
N/T |
N/T |
0.13 |
5.0 |
0.13 |
5.0 |
0.13 |
5.2 |
| 20 |
66 |
150 |
0.61 |
24.1 |
N/T |
N/T |
0.68 |
26.7 |
0.53 |
21.0 |
1.00 |
39.3 |
| Acetic Acid |
99 |
Boiling |
<0.01 |
<0.1 |
<0.01 |
0.1 |
<0.01 |
0.1 |
<0.01 |
0.1 |
<0.01 |
0.1 |
| Formic Acid |
88 |
Boiling |
0.01 |
0.4 |
0.05 |
2.0 |
0.02 |
0.9 |
0.04 |
1.4 |
0.24 |
9.3 |
| ASTM G 28A** |
|
Boiling |
0.67 |
26.3 |
3.52 |
138.6 |
1.02 |
40.0 |
5.97 |
235.0 |
0.48 |
18.8 |
| ASTM G 28B*** |
|
Boiling |
0.11 |
4.2 |
N/T |
N/T |
0.20 |
8.0 |
1.23 |
48.3 |
N/T |
N/T |
|
*N/T = not tested
**G 28A = 50% H2SO4 + 42 g/l Fe2(SO4)3
***G 28B = 23% H2SO4 + 1.2% HCl + 1% FeCl3 + 1% CuCl2
|
| Stress Corrosion Cracking |
A common solution for assessing the resistance to chloride-induced stress corrosion cracking of a material is boiling 45% magnesium chloride. This table indicates the times required to induce cracking in U-bend samples of several materials. The tests were stopped after six weeks (1008 hours).
|
Alloy |
Time to Cracking |
316L |
2 h |
254SMO |
24 h |
625 |
No cracking in 1008 h |
C-22 |
No cracking in 1008 h |
C-276 |
No cracking in 1008 h |
C-2000 |
No cracking in 1008 h |
|