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Reactor | M_init (g) | Q (L/min) | Res.Time | T_obs (hr) | T(hr) | Mexit/ | Vb | Vbottom |
---|---|---|---|---|---|---|---|---|
HalfCone | 400 | 0.6 | 12.48 | 9 | 12.56 0.72 |
| 84.9 | |
Funnel | 200 | 0.1 | 46.10 | 20 | 37.67 0.53 | 0.71 | 12.4 | |
Funnel | 200 | 0.1 | 46.10 | 25 | 37.67 0.66 | 0.71 | 12.4 | |
Funnel | 100 | 0.1 | 46.10 | 7.75 | 18.84 0.41 |
| 12.4 | |
Cone | 300 | 0.4 | 31.95 | 6 | 10.69 | 0.56 | 1.5 | 19.6 |
Cone | 300 | 1 | 12.78 | 1.25 | 4.28 0.29 |
| 49.0 | |
Cone | 500 | 0.88 | 14.52 | 4.75 | 8.10 | 0.59 | 2.35 | 43.1 |
Cone | 1800 | 0.55 | 23.24 | 18 | 46.65 0.39 |
| 26.9 | |
Cone | 1000 | 0.52/0.84 | 22.02 | 11 |
| 0.47 |
|
|
Cone | 1000 | 0.67 | 20.00 | 12 |
| 0.56 | 1.65 | 32.8 |
Table 1. Results of 2006 Experiments. M_init is the initial mass of lime; Q is the flow rate; T_obs is the time the effluent had a pH of 12; T is the theoretical duration; Vb is the upflow velocity; and Vbottom is the velocity at the bottom of the vessel.
ALKALINITY IN HONDURAN WATER
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