Recycling Treated Municipal Wastewater for Industrial Water Use

Recycling Treated Municipal Wastewater for Industrial Water Use Recycling Treated Municipal Wastewater for Industrial Water Use

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Cost Curves as Basis for Tertiary 1-Conventional Treatment Costs* Coagulant Addition/Flocculation/Sedimentation Capital Cost Design Flow Capital Cost (mgd) ($) 0.0001 $1,200,000 0.007 $1,200,000 0.022 $1,200,000 0.037 $1,200,000 0.091 $1,200,000 0.18 $1,200,000 0.27 $1,200,000 0.36 $1,200,000 0.68 $1,200,000 1 $1,326,582 1.2 $1,405,696 2 $1,722,152 3.5 $2,315,506 7 $3,700,000 17 $6,859,420 22 $8,439,130 76 $25,500,000 210 $67,836,232 430 $137,343,478 520 $165,778,261 1,500.00 $475,401,449 Cost, $ Cost, $ $5,000,000 $4,000,000 $3,000,000 $2,000,000 $1,000,000 $0 $30,000,000 $25,000,000 $20,000,000 $15,000,000 $10,000,000 $5,000,000 $0 y = 395569.63x + 931012.51 R 2 = 1.00 0 2 4 6 8 10 Flow, mgd y = 315942.03x + 1488405.54 R 2 = 1.00 0 10 20 30 40 Flow, mgd 50 60 70 80 Curve fit equations CCI Index 1.16 Avg Flow Range (O&M) 0.23-3.0 mgd >3-30 mgd Design Flow Range (Capital) 0.68-07.0 mgd >7-60 mgd Design/Avg Flow Ratio 2 Note: Adustments were made with vendor supplied costs for lower flows and to evaluate application of these costs for treated wastewater effluent (developed for potable supply). *Source: Environmental Protection Agency (EPA), 2003. Technologies and Costs Document for the Final Long Term 2 Enhanced Surface Water Treatment Rule and Final Stage 2 Disinfectants and Disinfection Byproducts Rule. December. EPA 815-R-05-013. Conventional Treatment.xls, Summ-Sed Page 1 of 2 5/3/2007 1:22 PM

Cost Curves as Basis for Tertiary 1-Conventional Treatment Costs* Coagulant Addition/Flocculation/Sedimentation O&M Cost Design Flow O&M Cost (mgd) ($) 0.00005 $37,000 0.0015 $37,000 0.0054 $37,000 0.0095 $37,000 0.025 $37,000 0.054 $37,000 0.084 $37,000 0.11 $37,000 0.23 $37,000 0.35 $40,552 0.41 $42,329 0.77 $52,986 1.4 $71,635 3 $119,000 7.8 $179,480 11 $219,800 38 $560,000 120 $1,593,200 270 $3,483,200 350 $4,491,200 750 $9,531,200 Cost, $ Cost, $ $140,000 $120,000 $100,000 $80,000 $60,000 $40,000 $20,000 $0 $600,000 $500,000 $400,000 $300,000 $200,000 $100,000 $0 y = 29602.83x + 30191.43 R 2 = 1.00 0 0.5 1 1.5 2 2.5 3 3.5 Flow, mgd y = 12600.00x + 81200.00 R 2 = 1.00 0 5 10 15 20 Flow, mgd 25 30 35 40 *Source: Environmental Protection Agency (EPA), 2003. Technologies and Costs Document for the Final Long Term 2 Enhanced Surface Water Treatment Rule and Final Stage 2 Disinfectants and Disinfection Byproducts Rule. December. EPA 815-R-05-013. Conventional Treatment.xls, Summ-Sed Page 2 of 2 5/3/2007 1:22 PM

Cost Curves as Basis <strong>for</strong> Tertiary 1-Conventional Treatment Costs*<br />

Coagulant Addition/Flocculation/Sedimentation<br />

O&M Cost<br />

Design<br />

Flow<br />

O&M Cost<br />

(mgd) ($)<br />

0.00005 $37,000<br />

0.0015 $37,000<br />

0.0054 $37,000<br />

0.0095 $37,000<br />

0.025 $37,000<br />

0.054 $37,000<br />

0.084 $37,000<br />

0.11 $37,000<br />

0.23 $37,000<br />

0.35 $40,552<br />

0.41 $42,329<br />

0.77 $52,986<br />

1.4 $71,635<br />

3 $119,000<br />

7.8 $179,480<br />

11 $219,800<br />

38 $560,000<br />

120 $1,593,200<br />

270 $3,483,200<br />

350 $4,491,200<br />

750 $9,531,200<br />

Cost, $<br />

Cost, $<br />

$140,000<br />

$120,000<br />

$100,000<br />

$80,000<br />

$60,000<br />

$40,000<br />

$20,000<br />

$0<br />

$600,000<br />

$500,000<br />

$400,000<br />

$300,000<br />

$200,000<br />

$100,000<br />

$0<br />

y = 29602.83x + 30191.43<br />

R 2 = 1.00<br />

0 0.5 1 1.5 2 2.5 3 3.5<br />

Flow, mgd<br />

y = 12600.00x + 81200.00<br />

R 2 = 1.00<br />

0 5 10 15 20<br />

Flow, mgd<br />

25 30 35 40<br />

*Source: Environmental Protection Agency (EPA), 2003. Technologies and Costs Document <strong>for</strong> the Final Long Term 2<br />

Enhanced Surface <strong>Water</strong> Treatment Rule and Final Stage 2 Disinfectants and Disinfection Byproducts Rule. December.<br />

EPA 815-R-05-013.<br />

Conventional Treatment.xls, Summ-Sed Page 2 of 2 5/3/2007 1:22 PM

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