In: Chemistry
Fresh feed containing 55 wt% A and 45 wt% B flowing at 100kg/h enters a separation system that removes a portion of pure component A only, as a bottom product. The top product stream (tops) of the separator unit contains 10 wt% of componenet A and the balance is B. A small part of the tops stream is recycled and mixed with the fresh feed stream- the remainder of the tops stream is purged. The separtor is designed to removed exactly two-thirds of component A that is fed into it. Determine the recycle ration (that is the ratio of the flow of the recycle stream to the flow of the fresh feed stream).
100 kg/h of fresh feed
Overall process
Total mass balance
100 = m6 + m4
Component balance (A):
Input = Output
0.55 * 100 = m6 + 0.1 m4
substituting m6 from overall balance equation
0.55 * 100 = (100 - m4) + 0.1 m4
55 = 100 - 0.9 m4
0.9 m4 = 100 - 55
0.9 m4 = 45
m4 = 50 kg/h
similarly for m6
100 = m6 + m4
substituting the value of m4, we get,
100 = m6 + 50
m6 = 50 kg/h
System separator
Total mass balance
m2 = 50 + m3
Component balance (A):
Input = Output
x A,2m2 = 50 + m3 (0.1)
Separator removed 2 / 3 of A fed to it in the bottom stream
from the component balance and the relation
75 = 50 + m3 (0.1)
m3(0.1) = 25
m3 = 250 kg/h
substituting m3 = 250 kg/h into overall mass balance equation arounf the separator
m2 = 50 + m3
m2 = 50 + 250
m2 = 300 kg/h
overall mass balance in spiltter
m3 = m4 + m5
250 = 50 + m5
m5 = 200 kg/h