|
QUESTIONS
FOR PUPILS
LPG
A)
As
you can see from the diagram two feed streams of crude oil
1 and 2 are flowing into the distillation column. By heating
the mixture the distillation column will separate the streams
into three components, LPG, LVN and Petrol.
Crude
oils vary enormously and we do not know the percentage of
each of the three components in each input stream, but we
can measure how much of each component comes out of the distillation
column.
We
need to work out the input percentages A, B, C and X, Y, Z
so that we can ensure that the correct mix of crude1 : crude2
is being fed in to the column.
We
can alter the rate at which each of the crude oils flow into
the column.
We
then measure how much of LPG, LVN and Petrol comes out for
that particular case.
The
information below shows two cases. The first case has crude
1 and 2 both flowing in at 100 m³/hr and the second has crude
1 at 200 m³/hr and crude 2 at 150 m³/hr.
Using
the information below produce three sets of simultaneous equations
and hence calculates the percentages A, B, C, X, Y and Z.
|
|
Crude
Oil
(m3/hr)
|
Total
in
|
|
Outputs
|
(m3/hr)
|
Total
out
|
| |
Stream
1
|
Stream
2
|
|
LPG
|
LVN
|
Petrol
|
|
|
Case
1
|
100
|
100
|
200
|
15
|
50
|
135
|
200
|
|
Case
2
|
200
|
150
|
350
|
25
|
87.5
|
237.5
|
350
|
CASE
1
CASE
2

B)
Following
the worked example now look at the financial implications
for running the distillation column using case2 i.e. 130 m3/hr
of crude 1 and 150 m3/hr of crude 2.
| |
Crude
1
|
Crude
2
|
Total
|
LPG
|
LVN
|
Petrol
|
Total
|
|
Case
2
|
130
|
150
|
280
|
34.5
|
62.5
|
183
|
280
|
The values
and costs remain the same
| If
the products are worth |
|
LPG $10
/m3 |
| |
|
LVN $20
/m3 |
| |
|
Petrol $30
/m3 |
| Crude
1 costs |
$15
/m3 |
|
| Crude
2 costs |
$25
/m3 |
|
How much
profit will you make? Which way would you run the process?
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