Regl. 3215, art. 5.2.3
Then calculate the F. factor as
Length: 1,392 wordsOfficial source
Cite as Reglamento Núm. 3215, Art. 5.2.3
follows:
0.209 F.
F.=
Eq. 3-4
F.
Calculated F. values beyond the
acceptable ranges shown in this table should
be investigated before accepting the test
results. For example, the strength of the
solutions in the gae analyzer and the
analyzing technique should be checked by
sampling and analyzing a known
concentration. such as air. the fuel factor
should be reviewed and verified. An
acceptability range of +12 percent is
appropriate for the F. factor of mixed fuels
with variable fuel ratios. The level of the
emission rate relative to the compliance level
should be considered in determining if a
relest is appropriate, i.e., if the measured
emissions are much lower or much greater
than the compliance limit. repetition of the
test would not significantly change the
compliance status of the source and would be
unnecessarily time-consuming and costly.
Fuel type
F,range
Coal:
Anthracte and a
1.016-1.130
a
1.083-1.230
Oil:
Distillate
1,260-1.413
Residual
1.210-1.370
Gas:
Natural
1.600-1.836
Propane
1434-1.586
Butane
1,406-1.553
Wood
1.000-1.120
Wood bank
1.003-1,130
5. Leak-Check Procedure for Orsat Analyzers
Moving an Orsat analyzer frequently
causes it to leak. Therefore. an Orsat analyzer should be throughly leak-checked on
site before the flue gas sample is introduced
into it. The procedure for leak-checking an
Orsat analyzer is:
5.1.1 Bring the liquid level in each plpette up to the reference mark on the capillary tubing and then close the pipette stopcock.
5.1.2 Raise the leveling bulb sufficiently
to bring the confining liquid meniscus onto
the graduated portion of the burette and
then close the manifold stopcock.
5.1.3 Record the meniscus position.
5.1.4 Observe the menicus in the burette
and the liquid level in the pipette for movement over the next 4 minutes.
5.1.5 For the Orsat analyzer to pass the
leak-check. two conditions must be met.
5.1.5.1 The liquid level in each pipette
must not fall below the bottom of the capillary tubing during this 4-minute interval.
5.1.5.2 The meniscus in the burette must
not change by more than 0.2 ml during this
4-minute interval.
5.1.6 If the analyzer fails the leak-check
procedure. all rubber connections and stop.
cocks should be checked until the cause of
the leak is identified. Leaking stopcocks
must be disassembled. cleaned. and regreased. Leaking rubber connections must
be replaced. After the analyzer is reassembled. the leak-check procedure must be repeated.
[Appendix A, Method 4)
11-25-83
Published by THE BUREAU OF NATIONAL AFFAIRS. INC., Washington. D.G. 20037
121:1574.2
FEDERAL REGULATIONS
6. Calculations
6.1 Nomenclature.
Ma=Dry molecular weight, g/g-mole (lb/lb.
mole).
= Percent excess air.
%CO,=Percent CO, by volume (dry basis).
%O,=Percent O, by volume (dry basis).
%CO Percent CO by volume (dry basis).
%N, Percent N, by volume (dry basis).
0.264=Ratio of O, to N, in air. v/v.
0.280 Molecular weight of N, or CO. divided by 100.
0.320=Molecular weight of O, divided by
100.
0.440 Molecular weight of CO, divided by
100.
6.2 Percent Excess Air. Calculate the percent excess air (if applicable), by substituting the appropriate values of percent On
CO. and N, (obtained from Section 4.1.3 or
4.2.4) into Equation 3-1.
%O₂-0.5%CO
%EA=
100
0.264
Equation 3-1
NOTE: The equation above assumes that
ambient air is used as the source of O2 and
that the fuel does not contain appreciable
amounts of N. (as do coke oven or blast furnace gases). For those cases when appreciable amounts of N, are present (coal, oil, and
natural gas do not contain appreciable
amounts of N,) or when oxygen enrichment
is used. alternate methods, subject to approval of the Administrator, are required.
6.3 Dry Molecular Weight. Use Equation
3-2 to calculate the dry molecular weight of
the stack gas
NOTE: The above equation does not consider argon in air (about 0.9 percent. moleculars weight of 37.7). A negative error of
about 0.4 percent is introduced. The tester
may opt to include argon in the analysis
using procedures subject to approval of the
Administrator.
7. Bibliography
0.280(%N,+%CO)
Equation 3-2
1. Altshuller, A. P. Storage of Gases and
Vapors in Plastic Bags. International Journal of Air and Water Pollution. 6.75-81.
1963.
2. Conner, William D. and J. S. Nader. Air
Sampling with Plastice Bags. Journal of the
American Industrial Hygiene Association.
25:291-297. 1964.
3. Burrell Manual for Gas Analysts, Sev.
enth edition. Burrell Corporation. 2223
Fifth Avenue, Pittsburgh. Pa. 15219. 1951.
4. Mitchell, W. J. and M. R. Midgett. Field
Reliability of the Orsat Analyzer. Journal
of Air Pollution Control Association 26:491-
495. May 1976.
5. Shigehara, R. T., R. M. Neulicht. and
W. S. Smith. Validating Orsat Analysis Data
from Fossil Fuel-Fired Units. Stack Sampling News. 4(2):21-26. August. 1976.
METHOD 4-DETERMINATION OF MOISTURE
CONTENT IN STACK GASES
1. Principle and Applicability
1.1 Principle. A gas sample is extracted
at a constant rate from the source: moisture
is removed from the sample stream and determined either volumetrically or gravimetrically.
1.2 Applicability. This method is applicable for determining the moisture content of
stack gas.
Two procedures are given. The first is a
reference method. for accurate determinstions of moisture content (such as are
needed to calculate emission data). The
second is an approximation method, which
provides estimates of percent moisture to
aid in setting isokinetic sampling rates prior
to a pollutant emission measurement run.
The approximation method described
herein is only a suggested approach: alternative means for approximating the moisture content, e.g.. drying tubes. wet bulb-dry
bulb techniques. condensation techniques,
stoichiometric calculations, previous expertence, etc., are also acceptable.
The reference method is often conducted
simultaneously with a pollutant emission
measurement run: when It is. calculation of
percent isokinetic, pollutant emission rate,
etc., for the run shall be based upon the results of the reference method or its equivalent: these calculations shall not be based
upon the results of the approximation
method. unless the approximation method
Is shown. to the satisfaction of the Administrator. U.S. Environmental Protection
Agency. to be capable of yielding results
within 1 percent H2O of the reference
method.
NOTE-The reference method may yield questionable
results when applied 10 saturated gas streatns or to
streams that contain water droplets. Therefore, when
these conditions exist or are suspected. a second deter.
mination of the moisture controt shall be made simpltaneously with the reference method, RS follows: Assime
that the gas stream is saturated. Attach a temperature
sensor (capable of measuring to *1° C (2° F)) to the
reference method probe. Measure the stack gas temperature at each traverse point (see Section 2.2.1) during the
reference method traverse; calculate the average stark
gas temperature. Next, determine the moisture percentage. either by: (1) using a psychrometric chart and
making appropriate corrections If stack pressure is
different from that of the chart. or (2) using saturation
vapor pressure tables. In cases where the psychrometric
chart or the saturation rapor pressure tables are not
applicable (based on evaluation of the process). alternate
methods, subject to the approval of the Administrator,
shall be used.
2. Reference Mithod
The procedure described in Method 5 for determining
moisture content is acceptable as a reference method.
2.1 Apparatus A schematic of the sampling train
used in this reference method is shown in Figure 4-1.
All components shall be maintained and calibrated
according to the procedure outlined in Method 5.
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