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Chemical Engineering Plant Economics

Chemical Engineering Plant Economics
With increase in the discounted cash flow rate of return, the ratio of the total present value to the initial investment of a given project

Increases
Increases linearly
Decreases
Remains constant

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Chemical Engineering Plant Economics
For a typical project, the cumulative cash flow is zero at the

End of the project life
Start up
Break even point
End of the design stage

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Chemical Engineering Plant Economics
The amount of compounded interest during 'n' interest periods is

P(1 + in)
P(1 - i)n
P(1 + i)n
P[(1+i)n-1)]

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Chemical Engineering Plant Economics
The economic life of a large chemical process plant as compared to a small chemical plant is

Much more
Only slightly more
Slightly less
Almost equal

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Chemical Engineering Plant Economics
Optimum economic pipe diameter for fluid is determined by the

Total cost considerations (pumping cost plus fixed cost of the pipe)
Viscosity of the fluid
Density of the fluid
None of these

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Chemical Engineering Plant Economics
Cost of piping in a fluid processing unit (e.g., distillation) of a chemical process plant is about __________ percent of the fixed capital investment.

22
34
4
13

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