E N D
1. Raccoon Mountain Team Hydrogen Production
Proposal
4-22-98
2. Outline Problem Statement
Flow Diagram
Material Balance
Equipment Design
Economic Analysis
Final Proposal
3. Problem Statement To design a plant which produces a required amount of hydrogen while minimizing costs and waste streams.
(Rev.3//2-26-98)
4. Flow Diagram
5. Flow Diagram
6. Material Balance (Target)
7. Equipment Design
8. Economic Analysis Reactor
100K gal. stainless steel
$215,000
9. Economic Analysis Hi Temp Shift Tank
100K gal. stainless steel
$175,000
10. Economic Analysis PSA System Tank (5)
500 gal. stainless steel (300psi)
$245,000
11. Economic Analysis Storage Tank (2)
50K gal. 304 stainless steel
$120,000
Heat Exchangers (2)
304 Stainless steel
w/.75” ODx1in. 1000ft2 area
$35,000
12. Economic Analysis
13. Economic Analysis Running Total $1,580,000
(Direct Plant Costs)
Engineering/Sup. (32%) $253,000
Construction (34%) $269,000
Subtotal $2,102,000
(Direct and Indirect Costs)
Contractor’s Fees (5%) $105,000
Contingency (10%) $210,000
Fixed Capital Investment $2,417,000
14. Economic Analysis COSTS
$3.50 / 1000cu.ft Natural Gas
$0.45 / 1000gal. H2O
$0.0758 / kwh Electricity
PROFITS
$0.40 / 100cu.ft Hydrogen Gas
Carbon Monoxide
Carbon Dioxide
15. Economic Analysis Fixed Capital Investment $2,417,000
Estimated Monthly Expenses $9,213,000
Estimated Monthly Profit $9,732,000
Estimated Yearly Profit $6,228,000
Estimated Recovery Period 10 months
Proposal
16. Economic Analysis
17. Conclusion