In: Economics
|
Continues stirred tank reactor |
First Cost, $ |
1000 |
Annual cost, $ per year |
400 |
Annual income, $ per year |
1600 |
Salvage value, $ |
2000 |
Life, Years |
5 |
Compressor |
|
First Cost, $ |
60,000 |
Annual operating cost, $ per year |
20,000 |
Salvage value, $ |
5000 |
Life, Years |
5 |
4.Heat exchanger has the following costs are under consideration for using in a new chemical plant. Using interest rate of 10% per year. Determine Annual worth.
Heat exchanger |
|
First Cost, $ |
20,000 |
Annual operating cost, $ per year |
12,000 |
Salvage value, $ |
74,300 |
Life, Years |
5 |
✓ If Ali invest $300,000 in a small project at an interest rate of 8% and another $600,000 in the same project at an interest rate of 10% then after 12 years Ali will receive -
$300,000*(1+ 0.08)^12 + $600,000*(1+0.1)^8
= $300,000*2.51817 + $600,000*1.85093
= $755,451 + $1,110,558
= $1,866,009 (Ans).
✓ Petrochemical manufacturing company is planning to increase production by replacing a new stirred tank reactor.
The PW of the tank reactor can be calculated as follows by PW(Cost ) and PW(Benefit). The Net Present Worth can be calculated as -
-$1000 - $1,000(P/F, 10%, 5) - $400(P/A, 10%, 10) + $1,600(P/A, 10%, 10) + $5,000(P/F, 10%, 5) + $5,000(P/F, 10%, 10)
(Note as the life is 5 years i.e why the tank reactor will be purchased two times because analysis period is 10 years)
= - $1,000 - $1,000/(1+0.1)^5 - $400[{(1+0.1)^10 - 1}/{0.1(1+0.1)^10}] + $1,600[{(1+0.1)^10 - 1}/{0.1(1+0.1)^10}] + $5,000/(1+0.1)^5 + $5,000/(1+0.1)^10
= -$1,000 - $620.92 - $400*6.1446 + $1,600*6.1446 + $3,104.60 + $1,927.72
= - $4,078.76 + $14,863.68
= $10,784.92 = $10,785 (Approx).
The NPW of 10 years working of tank reactor is $10,785 (Ans). We have PW Benefit and PW Cost together.
✓ Chemical Manufacturing expects cost of expanding operation section first cost is $40,000 and an annual operating cost of $9,000 and service life of 10 years.
We can calculate PW Cost at 10% interest is as follows -
$40,000 + $9,000*(P/A, 10%, 10)
= $40,000 + $9,000*6.1446 , [Discounting factor of (P/A, 10%, 10) = 6.1446 we have calculated it in above part]
= $40,000 + $55,301.4
= $95,301.4 = $95,301 (Approx).
There PW cost of expanding operation is $95,301. As it is cost we can represent it - $95,301 as NPW. The minus sign represent negative cash flow.
✓ The Annual Worth of Cost of compressor can be calculated as follows -
[$60,000 + $20,000(P/A, 10%, 5) - $5,000(P/F, 10%,5)]*(A/P, 10%, 5)
= [$60,000 + $20,000*{(1+0.1)^5 - 1}/{0.1(1+0.1)^5} - $5,000*(1+0.1)^-5]*[{0.1(1+0.1)^5}/{(1+0.1)^5 - 1}]
= [$60,000 + $20,000*3.7908 - $5,000*0.6209]*(0.2638)
= ($60,000 + $75,816 - $3104.5)*(0.2638)
= $132,711.5*0.2638
= $35,009.29 = $35,009 (Approx)
Therefore, AW Cost of compressor is $35,009 (Approx).
✓ AW Cost of Heat exchanger at 10% can be calculated as -
[$20,000 + $12,000(P/A, 10%, 5) - $74,300(P/F, 10%, 5)]*(A/P, 10%, 5)
[Note : The discounting factor (P/A, 10%, 5) = 3.7908 , (P/F, 10%, 5) = 0.6209 , (A/P, 10%, 5 = 0.2638 has been calculated above part]
= [$20,000 + $12,000*3.7908 - $74,300*0.6209]*(0.2638)
= ($19,356.73)*(0.2638)
= $5,106.30 = $5,106 (Approx).
Therefore, AW Cost of Heat exchanger is $5,106 (Approx).