Rule 1014. Reference method 5E, determination of particulate matter emissions from positive pressure fabric filters, reads as follows:
A range of nozzle sizes suitable for isokinetic sampling shall be available, for example, 0.32 to 1.27 cm (1/8 to 1/2 in.) or larger if higher volume sampling trains are used inside diameter (ID) nozzles in increments of 0.16 cm (1/16 in.). Each nozzle shall be calibrated according to the procedures outlined in subdivision (e) of this rule.
Sampling shall comply with the following provisions:
An = Cross-sectional area of nozzle, m2(ft.2).
A = Cross-sectional area of stack or flue at the point of sampling, ft2.
B ws = Water vapor in the gas stream, proportion by volume, expressed as a fraction.
B wi = Percent water vapor in gas entering source particulate control device determined by method 4.
B wo = Percent water vapor in gas exiting source particulate control device.
Ca = Wash blank residue concentration, mg/g.
Cs = Concentration of particulate matter in stack gas, pounds per 1,000 pounds of actual stack gas.
C sD = Concentration of particulate matter in stack gas, moisture excluded, pounds per 1000 pounds of dry stack gas.
Cs50 = Concentration of particulate matter corrected to 50% excess air, pounds per 1000 pounds of stack gas.
Cs50D = Concentration of particulate matter corrected to 50% excess air, excluding any water addition from a collector, pounds per 1000 pounds of stack gas.
E = Mass emission rate of particulate, lb/hr.
F50 = Concentration conversion factor to 50% excess air with no moisture alterations in exhaust.
F50D = Concentration conversion factor to 50% excess air, excluding any moisture added to exhaust gas by pollution collection system.
FD = Concentration conversion factor to dry basis, excluding any water in the stack gas.
I = Percent of isokinetic sampling.
L a = Maximum acceptable leakage rate for either a pretest leak check or for a leak check following a component change; equal to 0.00057 m3/min (0.02 cfm) or 4% of the average sampling rate, whichever is less.
Li = Individual leakage rate observed during the leak check conducted before the "ith" component change (i = 1, 2, 3 . . . . n), m3/min (cfm).
Lp = Leakage rate observed during the post-test leak check, m3/min (cfm).
Md = Molecular weight of dry stack gas, g/g mole (lb/lb-mole), calculated by method 3, equation 3-2, using data from integrated method 3.
mn = Total amount of particulate matter collected, mg.
Mw = Molecular weight of water, 18.0 g/g-mole (18.0 lb/lb-mole).
ma = Mass of residue of solvent after evaporation, mg.
mg = Total weight of gas samples through nozzle, lb.
P bar = Barometric pressure at the sampling site, mm Hg (in. Hg).
Ps = Absolute stack gas pressure.
Pstd = Standard absolute pressure, 760 mm Hg (29.92 in. Hg).
R = Ideal gas constant, 0.06236 mm Hg-m3/°K-g-mole (21.85 in.Hg-ft.3/°R?lb-mole).
Tm = Absolute average dry-gas meter temperature (see figure 104), °K (°R).
Ts = Absolute average stack gas temperature (see figure 104), °K (°R).
Tstd = Standard absolute temperature, 294.I°K (530°R).
V a = Volume of solvent blank, ml.
V aw = Volume of solvent used in wash, ml.
V lc = Total volume of liquid collected in impingers and silica gel (see figure 106), ml.
Vm = Volume of gas sample as measured by the dry-gas meter, dcm (dcf).
V m(std) = Volume of gas sample measured by the dry-gas meter, corrected to standard conditions, dscm (dscf).
V w(std) = Volume of water vapor in the gas sample, corrected to standard conditions, scm (scf).
Vs = Stack gas velocity, calculated by method 2, equation 2-9, using data obtained from method 5, m/sec (ft./sec).
Wa = Weight of residue in solvent wash, mg.
Y = Dry-gas meter calibration factor.
[DELTA]H = Average pressure differential across the orifice meter (see figure 104), mm H20 (in. H20).
%02 = Percent oxygen in stack gas by volume (dry basis).
%N2 = Percent nitrogen in stack gas by volume (dry basis).
p a = Density of solvent, mg/ml.
p s(std) = Density of all sampled gas at standard conditions, lb/ft.3;
pw = Density of water, 0.9982 g/ml (0.002201 lb/ml).
[THETA] = Total sample time, min.
[THETA]1 = Sample time, interval, from the beginning of a run until the first component change, min.
[THETA]i = Sampling time interval, between 2 successive component changes, beginning with the interval between the first and second changes, min.
[THETA]p = Sampling time interval, from the final (nth) component change until the end of the sampling run, min.
13.6 = Specific gravity of mercury.
60 = Sec/min.
100 = Conversion to percent.
386.9 = Cubic feet per lb-mole of ideal gas at standard conditions.
453.6 = Conversion of pounds to grams.
3600 = Conversion of hours to sec.
1000 = Conversion of 1000 lb units to lb units.
equation 5-1
Where:
K1 = 0.3869 °K/mm Hg for metric units.
[GREATER THAN EQUAL TO] 17.71 °R/in. Hg for English units.
Equation 5-1 can be used as written. However, if the leakage rate observed during any of the mandatory leak checks (for example, the post-test leak check or leak checks conducted before component changes) exceeds La, equation 5-1 shall be modified as follows:
and substitute only for those leakage rates (Li or Lp) that exceed La.
equation 5-2
Where:
K2 = 0.001338 m3/ml for metric units.
[GREATER THAN EQUAL TO] 0.04733 ft.3/ml for English units.
equation 5-3
In saturated or water droplet-laden gas streams, 2 calculations of the moisture content of the stack gas shall be made: 1 from the impinger analysis (equation 5-3), and a second from the assumption of saturated conditions. The lower of the 2 values of Bws shall be considered correct. The procedure for determining the moisture content based upon assumption of saturated conditions is given in the note of section 1.2 of method 4. For the purpose of this method, the average stack gas temperature from figure 104 may be used to make the determination, if the accuracy of the in-stack temperature sensor is ±1 degree Centigrade (2 degrees Fahrenheit).
equation 5-4
equation 5-5
Refer to subdivision (d)(iv)(E) of this rule to assist in the calculation of results involving 2 or more pairs of filters or 2 or more sampling trains.
equation 5-6
equation 5-7
equation 5-8
equation 5-9
equation 5-10
equation 5-11
equation 5-12
equation 5-13
equation 5-14
equation 5-15
Where:
K3 = 63.77 for English units.
Where:
Vf = Average gas velocity of the measurement site(s), m/sec (ft./sec).
Qi = Inlet gas volume flow rate, m3/sec (ft.3/sec).
Ao = Measurement site(s) total cross sectional area, m2(ft.2).
To = Temperature of gas at measurement site, °K (°R).
Ti = Temperature of gas at inlet, °K (°R).
Use the average velocity calculated for the measurement site in determining and maintaining isokinetic sampling rates.
All sources of gas leakage, into or out of the fabric filter housing between the inlet measurement site and the outlet measurement site, shall be blocked and made leaktight.
equation 5-16
Where:
K4 = 0.003458 mm Hg - m3;/ml - °K for metric units.
[GREATER THAN EQUAL TO] 0.002672 in. Hg - ft.3;/ml - °R for English units.
equation 5-17
Where:
K5 = 4.307 for metric units.
[GREATER THAN EQUAL TO] 0.09409 for English units.
Appendix A Method 5, August 18, 1977.
Equipment. Environmental Protection Agency. Research Triangle Park, N.C.APTD-0581. April, 1971.
Mich. Admin. Code R. 336.2014