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Demand Formula: Gr./hr = L/hr x O3D
Gr./hr = Grams of ozone per hour
L/hr = Liters per hour flow rate to be treated.
O3D = Ozone demand in mg/l to treat the contaminants in the water.
There are three basic steps to calculate the Gr./hr of Ozone needed to treat the water.
Step 1: Calculate the flow rate to be treated in L/hr.
If your data states the flow rate in gallons per minute you must multiply that rate by
60 to determine the equivalent flow rater in gallons per hour. Then multiply the gallons
per hour figure by 3.785 to determine the equivalent flow in L/hr.
Step 2: Determine the contaminant demand on ozone by multiplying the mg/l of each
contaminant found in your water and adding 0.5 mg/l for disinfection to the sum total.
Fe demand = X x 0.43 = mg/l
Mn demand = X x 0.87 = mg/l
H2S demand = X x 3.0 = mg/l
Tannins demand = X x 0.1 = mg/l
For Disinfection add 0.5 mg/l (add demands to get total demand)
Sum Total = mg/l = mg/l(O3) demand = O3D
Step 3: Multiply O3D by L/hr to calculate mg/hr
Step 4: Divide by 1000 to convert to grams per hour needed to treat the water.
Computation Example:
Water sample shows 1.7 mg/l Fe and the flow to be treated is 5 gpm;
Step 1: Convert gpm flow rate to liters per hour (l/h);
5 gpm x 60 x 3.785 = 1135.5 L/hr.
Step 2: Determine the contaminant demand on ozone;
1.7 mg/l Fe x 0.43 = 0.731 mg/l + 0.5 mg/l (for
disinfection) = 1.231
Step 3: Multiply O3D by rate of flow;
1,135.5 l/h x 1.231 mg/l = 1,397.8 mg/hr;
Step 4: Divide by 1000 to convert from milligrams to grams;
1,397.8 / 1000 = 1.4 gr./hr Total Ozone Demand.
Keep in mind that ozone will react first with H2S, then with Fe followed by
Mn and lastly with Tannins. There are other things, such as temperature of the water,
organically bound compounds, or seasonal variations that bear on the exact ozone treatment
system design. It would be sensible to figure a slightly higher (perhaps 20%) ozone demand
and increase contact time to factor in unknowns.
To treat surface waters some will say that having a residual of ozone after appropriate
contact time is all that is needed. We recommend that when treating surface waters with
bacteria, virus, or cysts and multiple other oxidizable contaminants that ozonation be a
two step process. In step one, ozonation and filtration will purify the water (remove
iron, manganese, hydrogen sulfide, etc.). In step two, ozone will again be injected and a
ozone residual will be maintained to insure disinfection. A possible alternative to the
second point of ozone injection could include the use of Giardia approved filter systems
or ultra-violet radiation post filtration.
3. Determine Equipment and Chemical needs
Each component of the ozone treatment system must be properly sized to work
together and produce treated water at the required rate of flow.
3.1. Ozone Injection
There is two most common methods of injecting ozone into the water, using a
pump to force ozone through a diffuser and venturi injection. We prefer venturi injection
because it is very efficient and requires no moving parts. Water pressure at the inlet of
the venturi injector must be higher than the outlet pressure during the entire pump cycle.
This difference is known as the pressure differential. The pressure differential required
for each treatment system is determined by two variables.
Variable 1.
Required rate of injection, stated as liters per minute (l/m) or equivalent Standard
Cubic Feet per Hour (SCFH). The required rate for your ozone generator can be obtained
from your ozone equipment or manufacturer. Request a chart showing various rates of ozone
production at various injection rates. Proper use of this information will enable a
certain amount of "customization" for each application.
Variable 2.
The selected venturi injector. Again, use the injector charts to select an injector
that meets or exceeds the required injection rate set by your ozone equipment
manufacturer.
3.2. Ozone Contact and off-gas.
After injection the ozone must have time to do its work. This time is known
as contact time. Contact time is the time ozone has to oxidize and disinfect or the time
the water is allowed to hold the disinfectant. For ozone, contact time is measured from
the point of injection to the filter. Depending upon the circumstances of each
installation, there may still be ozone in the water after filtration but for purposes of
calculating contact time, the filter marks the end. Suppose you inject ozone into a 25
gallon contact vessel followed by a filter and the flow rate is 5 gpm, the contact time in
this situation would be 25 gallons divided by 5 gallons per minute resulting in 5 minutes
contact time.
The contact time needed varies with the matter to be oxidized. Time required for
oxidation ranges from almost instantly to 10 minutes or more. A general rule of thumb is
no less than 4 minutes contact time with a measurable residual of 0.1-mg/l ozone and more
contact time is better. Dont take a good thing too far, because ozone is so fast
reacting and has such a short
life once generated it is possible to have too much contact
time in which case you wouldnt have a measurable residual.
There are several reasons more contact time is better, here are two;
1. Contaminants floc or precipitate at varying rates and with varying degrees of
density, giving more time will often make a treatment system a success by providing time
for material to fully precipitate which in turn enhances filterability.
2. Ozone must contact the contaminant to oxidize or disinfect; more contact time
increases the odds that all water will be subjected to oxidation.
If using ozone to disinfect, there are guidelines set by the Environmental Protection
Agency (EPA). The EPA has proposed the use of a "CT value" to assure the
attainment of primary disinfection at a minimum cost. The CT value is the numerical
product of the concentration of residual disinfectant ("C"), in mg/l, multiplied
by the time (T), in minutes, during which the residual is present.
C (mg/l) x T (min.) =
CT value (mg/l-min)
Thus, units for CT-values are expressed as mg/l-min.
CT tables show the required CT value at a given temperature and pH. To be more precise
and meet regulatory requirements please refer to the approved CT tables used by the
regulating authority in your area. Most agencies use the EPA recommended CT values.
All gasses inducted through the venturi must be properly disposed of or
"off-gassed". At a bare minimum, this is accomplished by simply venting the
contact tank to the outside. It may be required to route the gasses through an ozone
destruct unit to insure no ozone gasses are being emitted from the treatment system.
3.3. Filtration of oxidized particulate.
At O3 Water Systems we most often specify multi-media filtration
with our ozonation systems. In most cases, a properly sized multi-media depth filter is
very well suited to
filtering objectionable oxidized contaminants and will give years of
operation with little required maintenance. In some cases a series of filters will be
needed to accomplish adequate filtration. Circumstances (usually regulatory enforcement of
the SWTR) may require additional filtration to physically remove Giardia and/or
Cryptosporidium.
It is recommended that activated carbon filtration be used as a final filtration step
to remove any dissolved ozone potentially remaining in the water.
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