By using a time-lag technique, an investigation was made of H permeation through 18Cr-8%Ni steel plates as a function of the H pressure (0.1 to 30atm) at the entry surface, the temperature (300 to 800C), and the membrane thickness (0.0252 to 0.2475cm). The permeabilities were strongly dependent upon the H pressure, and this was attributed to aresistance to flow at the membrane surface, rather than to a concentration-dependent diffusivity of H in the steel (table 90). Overall, the data could be described by:
D (cm2/s) = 0.44 exp[-12.5(kcal/mol)/RT]
J.R.Phillips, B.F.Dodge: American Institute of Chemical Engineers Journal, 1968, 14[3], 392-7
Table 90
Permeation and Diffusion of H in 18Cr-8%Ni Steel
Thickness (cm) | Temperature (C) | H2 (atm) | P (cm3/min atm½) | D (cm2/s) |
0.1011 | 603 | 1.03 | 1.3 x 10-3 | 3.3 x 10-4 |
0.1011 | 603 | 10.9 | 1.2 x 10-2 | 3.3 x 10-4 |
0.1011 | 395 | 1.01 | 2.0 x 10-4 | 3.6 x 10-5 |
0.1011 | 395 | 10.2 | 7.5 x 10-4 | 3.6 x 10-5 |
0.1011 | 395 | 29.1 | 2.0 x 10-3 | 3.6 x 10-5 |
0.2475 | 398 | 1.04 | 5.9 x 10-5 | 3.6 x 10-5 |
0.2475 | 398 | 10.1 | 2.4 x 10-4 | 3.6 x 10-5 |
0.2475 | 398 | 30.4 | 9.1 x 10-4 | 3.6 x 10-5 |
0.1003 | 302 | 1.04 | 5.0 x 10-5 | 7.9 x 10-6 |
0.1003 | 302 | 30.1 | 8.0 x 10-5 | 7.9 x 10-6 |