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Product Viscosity vs. Shear

Vertical Tank Selection

Low Flow in Pipes- posted in Ankur's blog

Started by Hans Cholo Chua, Apr 17 2016 10:24 AM

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Posted 17 April 2016 - 10:24 AM

Can anyone post a step by step procedure for designing an Air stripping tower for Red Nitric Acid?

I Am only Given this data

Composition of Stream to be Purified:

Red Nitric Acid IN:

HNO3 = 23,371.20 kg/day

H2O = 15,580.80 kg/day

N2O4 = 2,050.11 kg/day

The Impurity to be stripped is N2O4..

Mass of Air IN = 24,132.08 kg/day

Concerns:

1. How can I calculate for the overall mass transfer coeffecient?

2. How can I calculate the actual flow rates of the streams and the capacity of the equipment?

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