Concentration
Minimum
Average
Maximum
------------------------------------------------------------
Fluoride (mg/L)
[_____]
[_____]
[_____]
[_____]
[_____]
[_____]
mg/L as CaCO3)
Dissolved oxygen (mg/L)
[_____]
[_____]
[_____]
Free chlorine residual (mg/L)
[_____]
[_____]
[_____]
Silica (mg/L)
[_____]
[_____]
[_____]
Total solids (mg/L)
[_____]
[_____]
[_____]
Total dissolved solids (mg/L)
[_____]
[_____]
[_____]
Suspended solids (mg/L)
[_____]
[_____]
[_____]
Turbidity in nephelometric
[_____]
[_____]
[_____]
turbidity units (NTU)
Color by platinum standard
[_____]
[_____]
[_____]
comparison
1.4.3
Performance Requirements
**************************************************************************
NOTE: Coordinate controls with the blower specified
in Section 11215A FANS/BLOWERS/PUMPS; OFF-GAS.
Select the retention time appropriate for the
oxidation device considering any regulated compounds.
**************************************************************************
[2.0] [2.5] [_____] seconds at [1095] [982] [820] [760] [400] [260] degrees
C [2,000] [1,800] [1,500] [1,400] [750] [500] degrees F minimum at maximum
flow. The flow rate shall be [constant at [_____] cu m/second scfm] [off
and on at [_____] cu m/second scfm maximum, with a turndown range of four
to one (4:1)] [variable between [_____] cu m/second scfm minimum and
[_____] cu m/second scfm maximum]. Flow rates shall be based on
measurement at standard temperature and pressure (STP), 101.3 kPa at 15.5
degrees C 14.7 psia at 60 degrees F. Influent gauge pressure shall vary
between [_____] Pa inches H2O minimum, [_____] Pa inches H2O average, and
[_____] Pa inches H2O maximum. Inlet temperature shall vary between
[_____] degrees C degrees F minimum, [_____] degrees C degrees F average
and [_____] degrees C degrees F maximum. Materials of construction shall
be compatible with the ambient and operating temperatures and long term
exposure to untreated and treated gas constituents.
1.4.4
**************************************************************************
NOTE: Reduce the dew point to below 50 degrees C
(120 degrees F) ahead of the thermal oxidizer.
If the unit will be classified as a hazardous waste
SECTION 11378
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