fundamentals of engineering supplied-reference handbook - Ventech!
fundamentals of engineering supplied-reference handbook - Ventech!
fundamentals of engineering supplied-reference handbook - Ventech!
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Bed Expansion<br />
Monosized Multisized<br />
Lo<br />
( 1−<br />
ηo<br />
)<br />
L fb =<br />
L = ( 1−<br />
η )∑<br />
0.<br />
22 fb Lo<br />
o<br />
⎛V<br />
⎞<br />
1−<br />
⎜ B<br />
⎟<br />
⎝ Vt<br />
⎠<br />
0. 22<br />
⎛ VB<br />
⎞<br />
η fb = ⎜ ⎟<br />
⎜ V ⎟<br />
, where<br />
t<br />
⎝<br />
⎠<br />
Lfb = depth <strong>of</strong> fluidized filter media (m),<br />
VB = backwash velocity (m/s), Q/Aplan,<br />
Vt = terminal setting velocity, and<br />
ηfb = porosity <strong>of</strong> fluidized bed.<br />
Lo = initial bed depth<br />
ηo = initial bed porosity<br />
Lime-Soda S<strong>of</strong>tening Equations<br />
50 mg/L as CaCO3 equivalent = 1 meq/L<br />
1. Carbon dioxide removal<br />
CO2 + Ca (OH)2 → CaCO3(s) + H2O<br />
x<br />
⎛<br />
⎜<br />
V<br />
1−<br />
⎜<br />
⎝<br />
Vt,<br />
ij<br />
B<br />
i,<br />
j<br />
2. Calcium carbonate hardness removal<br />
Ca (HCO3)2 + Ca (OH)2 → 2CaCO3(s) + 2H2O<br />
3. Calcium non-carbonate hardness removal<br />
CaSO4 + Na2CO3 → CaCO3(s) + 2Na + + SO4 –2<br />
4. Magnesium carbonate hardness removal<br />
Mg(HCO3)2 + 2Ca(OH)2 → 2CaCO3(s) +<br />
Mg(OH)2(s) + 2H2O<br />
5. Magnesium non-carbonate hardness removal<br />
MgSO4 + Ca(OH)2 + Na2CO3 → CaCO3(s) +<br />
Mg(OH)2(s) + 2Na + + SO4 2–<br />
6. Destruction <strong>of</strong> excess alkalinity<br />
⎞<br />
⎟<br />
⎠<br />
0.<br />
22<br />
2HCO3 – + Ca(OH)2 → CaCO3(s) + CO3 2– + 2H2O<br />
7. Recarbonation<br />
Ca 2+ + 2OH – + CO2 → CaCO3(s) + H2O<br />
164<br />
Molecular<br />
Formulas<br />
CO3 2–<br />
CO2<br />
Ca(OH)2<br />
CaCO3<br />
Ca(HCO3)2<br />
CaSO4<br />
Ca 2+<br />
H +<br />
HCO3 –<br />
Mg(HCO3)2<br />
Mg(OH)2<br />
MgSO4<br />
Mg 2+<br />
Na +<br />
Na2CO3<br />
OH –<br />
SO4 2–<br />
ENVIRONMENTAL ENGINEERING (continued)<br />
Molecular<br />
Weight<br />
60.0<br />
44.0<br />
74.1<br />
100.1<br />
162.1<br />
136.1<br />
40.1<br />
1.0<br />
61.0<br />
146.3<br />
58.3<br />
120.4<br />
24.3<br />
23.0<br />
106.0<br />
17.0<br />
96.1<br />
n<br />
# Equiv per<br />
mole<br />
2<br />
2<br />
2<br />
2<br />
2<br />
2<br />
2<br />
1<br />
1<br />
2<br />
2<br />
2<br />
2<br />
1<br />
2<br />
1<br />
2<br />
Rapid Mix and Flocculator Design<br />
G =<br />
P<br />
=<br />
µ Vol<br />
γH<br />
L<br />
t µ<br />
Equivalent<br />
Weight<br />
30.0<br />
22.0<br />
37.1<br />
50.0<br />
81.1<br />
68.1<br />
20.0<br />
1.0<br />
61.0<br />
73.2<br />
29.2<br />
60.2<br />
12.2<br />
23.0<br />
53.0<br />
17.0<br />
48.0<br />
Gt = 10 4 − 10 5<br />
where<br />
G = mixing intensity = root mean square velocity<br />
gradient,<br />
P = power,<br />
Vol = volume,<br />
µ = bulk viscosity,<br />
γ = specific weight <strong>of</strong> water,<br />
HL = head loss in mixing zone, and<br />
t = time in mixing zone.<br />
Reel and Paddle<br />
P =<br />
C A ρ V<br />
2<br />
3<br />
D P f p<br />
,where<br />
CD = drag coefficient = 1.8 for flat blade with a<br />
L:W > 20:1,<br />
Ap = area <strong>of</strong> blade (m 2 ) perpendicular to the direction <strong>of</strong><br />
travel through the water,<br />
ρf = density <strong>of</strong> H2O (kg/m 3 ),<br />
V p = relative velocity <strong>of</strong> paddle (m/sec), and<br />
V mix = Vp • slip coefficient.<br />
slip coefficient = 0.5 − 0.75.