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Material Type: Assignment; Class: Environmental Engineering; Subject: Civil Engineering; University: Lafayette College; Term: Fall 2008;
Typology: Assignments
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HRT = Vol/Q = (140 ft17 ft18 ft)7.48 gal/ft 3 /2,000,000 gpd = 0.16 d = 3.85 hrs Surface loading rate = Q/As = 2,000,000 gpd1 day/(6024 min) / (17 ft140 ft) = 0.58 gpm/ft 2
Plug Flow Reactor: C = C 0 e-kHRT
Ln(C/C0) = - k HRT k = - Ln(C/C0)/HRT HRT = V/Q = 1.5 MG/8 MGD = 0.1875 days = 4.5 hrs So k = - Ln(C/C0)/HRT = -Ln(0.001)/4.5 hrs = 1.535 hr -
With short-circuiting, the new HRT is 2.5 hrs, so C/C 0 = e-1.535*2.5^ = 0.0215. Thus % removal is now = 97.85%
-7.
This is an aqueous acid-base equilibrium reaction: HOCl ↔ H+^ + OCL-^ K (^) A =10 -7.
The equilibrium expression is: K (^) A = [H+^ ][OCL-^ ] / [HOCl] So [OCL-^ ] / [HOCl] = 10 -7.5^ / [H+^ ]
Since pH = -log[H +^ ], you can plug in values for pH, and calculate the right hand side, which is the ratio you are looking for. When you plot these numbers, you'll find that [OCL-^ ] / [HOCl] = 1 at pH=pKA =7.5.
If pH < 7.5, the ratio is less than 1, and if pH > 7.5, the ratio is greater than 1. So lower pH (acidic) favors HOCl, which is the better disinfectant.
First find mg of OCl-^ needed: 2 mg/L * 5 gal * 3.785 L/gal = 37.85 mg OCl-
Now calculate how much NaOCl bleach you need to get 37.85 mg OCl-
NaOCl dissociates completely in water: NaOCl → Na+^ + OCl-
1000mg/g = 37.85 mg OCl-
X = 0.165 teaspoons (less than a quarter teaspoon). Note: this is less than the EPA estimate on the handout I gave you which is based on a higher dose. Remember that effectiveness depends on both dose and contact time (CT)
Q*C gives the mass flow rate (e.g., mass/time)
Ca+2: 120 mg/L x (1 mol Ca/40,100 mg Ca) x (1 mol lime/1 mol Ca) x (74,100 mg Lime/mol lime) x ( kg/1,000,000 mg) x (3,000,000 gal/day) x (3.785 L/gal) = 2,518 kg/day (a lot)
Mg+2: 50 mg/L x (1 mol Mg/24,300 mg Mg) x (2 mol lime/1 mol Mg) x (74,100 mg Lime/mol lime) x ( kg/1,000,000 mg) x (3,000,000 gal/day) x (3.785 L/gal) = 3,463 kg/day (even more!)
Total = 5981 kg/day
Just for context, Q = 0.8 m^3 /s = 18.25 MGD = more than twice the size of Easton WTP
SLR = 110 m^3 /d/sq m = Q/As = 0.8 m^3 /s86,400 s/day/(N10mX10m) N = 6.28 so use 7. But you could likely get by with 6 because 110 m^3 /d/sq m is a conservative SLR for filtration (see p436 of text and class notes giving typical SLRs of 2-4 gpm/sq ft which works out to 120-240 m 3 /d/sq m ) For N = 6 we would have an SLR of 115 m 3 /d/sq m, which is still at the low end of the range.
SLR =300 m^3 /d/sq m = 0.8 m 3 /s86,400 s/day/(N10mX10m) N = 2.3 This is not many filters for a pretty large treatment plant. Text (see p436) suggests a minimum of 4 filters for large (Q > 0.5 m^3 /s) treatment plants, so use N = 4
Using the data in Table 10-4, we need at CT value of 144 mg/L*min for the conditions in the problem (3-log removal = 99.9% removal). Since C = 1.20 mg/L, then T = HRT = 144/1.2 = 120 min or 2 hrs
Vol = HRT*Q = 120 min * 2.409 m 3 /s * 60 s/min = 17,345 m 3 (= 4.5 million gals – that’s a big tank but Q is very large – about 55 MGD)