28.02.2013 Views

Handbook of Solvents - George Wypych - ChemTech - Ventech!

Handbook of Solvents - George Wypych - ChemTech - Ventech!

Handbook of Solvents - George Wypych - ChemTech - Ventech!

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

22.4 Application <strong>of</strong> solar photocatalytic oxidation 1569<br />

Table 22.4.3. Comparison <strong>of</strong> estimated costs for similarly sized PCO, carbon<br />

adsorption, and thermal oxidation VOC treatment systems<br />

Direct Costs<br />

Purchased Equipment (PE)<br />

Photoreactor 1<br />

Condenser/Chiller 2<br />

Instrumented<br />

Blower/Scrubber Skid 3<br />

Total PE (TPE) 4<br />

Installation<br />

Solar PCO<br />

non-concentrating<br />

14,000<br />

10,625<br />

60,000<br />

91,395<br />

27,419<br />

Carbon Adsorption<br />

74,500 5<br />

22,350<br />

Thermal Oxidation<br />

100,500 5<br />

30,150<br />

Total Direct Costs 118,814 96,850 130,650<br />

Indirect Costs<br />

Indirect Installation Costs 7 29,923 24,391 32,904<br />

Total Capital Required 8<br />

Operating Costs<br />

148,736 121,241 163,554<br />

9<br />

Electricity<br />

Fuel 10<br />

2,880<br />

1,440<br />

1,440<br />

0<br />

0<br />

5,000<br />

Maintenance, Labor and Material 20,376<br />

19,308<br />

20,952<br />

Direct Annual Costs<br />

23,256<br />

25,748<br />

27,392<br />

Indirect Annual Costs<br />

8,664<br />

7,063<br />

9,527<br />

Total Annual Costs 31,920 32,811 36,919<br />

Levelized Cost 12<br />

56,135 25,549 63,456<br />

Levelized Cost/CFM 281 263 318<br />

1<br />

IST Corp., Golden, CO. Non-concentrating reactor cost is current and estimated price reductions anticipated from<br />

economies <strong>of</strong> scale at higher production levels.<br />

2<br />

Peters and Timmerhaus, 1991.<br />

3<br />

Zentox Corp., Ocala, FL. Concentrating vs. non-concentrating is primarily a function <strong>of</strong> instrumentation level.<br />

4<br />

Includes 0.08 x PE for taxes and freight (Vatavuk, 1994).<br />

5<br />

Calculated using EPAs HAPPRO v.2.1 s<strong>of</strong>tware.<br />

6<br />

0.38 x PE (Vatavuk, 1994).<br />

7<br />

0.28 x TPE, including engineering costs, construction fee, and start-up costs (Vatavuk, 1994)<br />

8<br />

Includes 6% contingency.<br />

9<br />

Based on $0.08/kWh, 10 kW blower and chiller costs.<br />

10<br />

Based on $0.33/ccf natural gas.<br />

11<br />

0.06 x Total Capital Required for taxes, insurance, and administration.<br />

12<br />

Based on 10% interest rate, 10 year depreciation.<br />

REFERENCES<br />

Ayer, J. and Darvin, C. H., 1995, “Cost Effective VOC Emission Control Strategies for Military, Aerospace, and<br />

Industrial Paint Spray Booth Operations: Combining Improved Ventilation Systems with Innovative, Low-Cost<br />

Emission Control Technologies”, Proceedings <strong>of</strong> the 88th Annual Meeting <strong>of</strong> the Air and Waste Management Association,<br />

Vol. 4B, 95-WA77A.02.<br />

Blake, D.M., 1996, Bibliography <strong>of</strong> Work on the Heterogenous Photocatalytic Removal <strong>of</strong> Hazardous Compounds<br />

from Water and Air, Update Number 2 to October 1996. NREL/TP-430-22197. Golden, CO: National Renewable<br />

Energy Laboratory.<br />

Bekbolet, M. and Balcioglu, I., 1996, Water Science and Technology, Vol. 34, No. 9, pp. 73-80.

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!