Hi All,
I have been asked to extend a pipe line from one of our scrubbers to a packing point in the plant, this may require a greater strength fan and i was wandering whether a local extraction point with no scrubber would be more cost effective.
I am dealing with 70% strength Nitric acid and in order to see whether this option is safe i need to know how to calculate the evaporation rate of the acid and compare to those allowed by the HSE. Do you know how I can determine this value?
Thanks for your time
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Evaporation Rate Of Nitric Acid
Started by jimjones, Dec 16 2008 09:49 AM
1 reply to this topic
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#1
Posted 16 December 2008 - 09:49 AM
#2
Posted 16 December 2008 - 06:43 PM
Found this paper on the net that looks like it could be just what you're looking for:
Fermilab Paper
Vapor generation and mist evaporation during Buffered Chemical Polish (BCP) operations at the Material Development Testing Laboratory (MDTL)
D. Baird, C. Boffo*, C. Cooper, R. Ruthe
January 17, 2007
All the best with this.
My initial thoughts are that you want to be very sure of your design given the toxicity of 70% HNO3. With material like this, erring on the side of safety is going to keep everybody happy.
Fermilab Paper
Vapor generation and mist evaporation during Buffered Chemical Polish (BCP) operations at the Material Development Testing Laboratory (MDTL)
D. Baird, C. Boffo*, C. Cooper, R. Ruthe
January 17, 2007
All the best with this.
My initial thoughts are that you want to be very sure of your design given the toxicity of 70% HNO3. With material like this, erring on the side of safety is going to keep everybody happy.
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