In this article i am going to share with you how we can calculate Material Balance Without chemical reaction. For this please read below.
A two stage membrane process is designed for separation of carbon monoxide from a mixture of Carbon monoxide (47% mole basis) and rest Hydrogen. The system is designed to recover 93.2% CO with 98% mole% purity. Recycle stream is kept at 5000 mol/h for a fresh feed rate of 500 mol/h. This requirement is stipulated to achieve 1.1 mole ratio of Hydrogen / Carbon monoxide in the feed to second stage. In this we will find,
1) The flow rates of product CO stream.
2) Composition of product H2 stream.
SOLUTION :
Fresh Feed F = 5000 mol/h
1) CO in fresh feed at the rate of 47% = 5000 * 0.47
= 2350 mol/h
H2 in fresh feed at the rate 53% = 2650 mol/h
CO in product stream for 93.2% recovery = 2350 * 0.932
= 2190.2 mol/h
Product CO stream = 2190.2 / 0.98 = 2234.9 mol/h
2) H2 in CO stream = 2234.9 - 2190.2
= 44.7 mol/h
Mole of H2 in product H2 stream = 2650 - 44.7
= 2605.3 mol/h
Moles of CO in product CO stream = 2350 - 2190.2
= 159.8 mol/h
Mole % of H2 in product H2 stream = (2605.3 / 2605.3+159.8) * 100
=94.2%
Mole % of CO in product CO stream = 100 - 94.2
=5.8%