plantprowler
Chemical
- Aug 10, 2013
- 136
What are possible pump MOC choices for a hot (90 C) NaCl brine duty. The brine is saturated approx. 27% w/w. Due to the chloride crevice corrosion / pitting potential of NaCl I'm not sure what might be a cost effective MOC selection?
The pump is relatively small in capacity & has only a very modest head requirement. i.e. 50 m3/hr @ 20 m differential head.
The pump is relatively small in capacity & has only a very modest head requirement. i.e. 50 m3/hr @ 20 m differential head.