kellys13
Chemical
- Feb 6, 2006
- 1
Am having a discussion regarding our USP water for injection distribution and storage system.
System currently meets USP compendial requirements for water for injection (WFI). It was installed in a GMP fashion, 316L SS throughout (15Ra internal finish) (cleaned, degreased, passivated prior to startup). This is a hot system (80C).
Questions:
1) Will blanketing WFI storage tank with N2 increase the rate of rouge formation throughout the distribution system?
2) Should the initial passive layer be viewed as a dynamic layer, fluctuating depending on the amount of dissolved O2 in the liquid stream, or a single starting point from which degradation occurs?
System currently meets USP compendial requirements for water for injection (WFI). It was installed in a GMP fashion, 316L SS throughout (15Ra internal finish) (cleaned, degreased, passivated prior to startup). This is a hot system (80C).
Questions:
1) Will blanketing WFI storage tank with N2 increase the rate of rouge formation throughout the distribution system?
2) Should the initial passive layer be viewed as a dynamic layer, fluctuating depending on the amount of dissolved O2 in the liquid stream, or a single starting point from which degradation occurs?