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#1
Posted 26 September 2011 - 01:07 PM
#2
Posted 15 October 2011 - 09:40 PM
Can you please provide the following information:
1) Design pressure of your tank. Both positive and negative
2) maximum quench water flowrate
3) A possible sketch of the spray system for water inside the tank
4) size of tank
5) any insulation?
Although it may not be possible to accurately estimate how quick the steam generated in the CIP stage is condensed in the cooling phase, we may be able to take a conservative approach and based on contact condensation heat transfer coefficients and calculate a rate of condensation.
Please provide the above info so I can look into this further
#3
Posted 20 February 2013 - 07:27 AM
Hi there, I have a similar issue, with smaller tanks.
Between 20 and 170 m3. Some tanks chilled water jacketed, some just insulated. Depending on which are of our factory, rinse flowrates vary and CIP temperature vary but principle is the same, looking for a method rather than an answer for a specific case (we have had an issue with a tank imploding due to blocked vent, and another one that is creaking a bit! - rather than just blanket "make all teh vents bigger" I want to have some form of basis of design...)
All are "atmospheric" tanks (i.e. not pressure or vacuum rated).
Hot CIP followed by cold rinse = vaccum risk
How do I size the vent? (other than making it "bloody big") - OK so I don't have an expensive valve to size as the tank is open to atmosphere anyway, but I don't want a HUGE vent as there are implications on tank top layout, vent cleaning (food product, don't want muck in the vent) etc etc.
Any help appreciated!
#4
Posted 21 February 2013 - 06:26 AM
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