Current through August 26, 2024
(1) APPLICABILITY
AND DESIGNATION OF AFFECTED FACILITY.
(a) The
affected facility to which the provisions of this section apply is each rotary
spin wool fiberglass insulation manufacturing line.
(b) The owner or operator of any facility
under par. (a) that commences construction, modification, or reconstruction
after February 7, 1984, is subject to the requirements of this section.
(2) DEFINITIONS. As
used in this section, terms not defined in this subsection have the meanings
given in s.
NR 440.02.
(a) "Glass
pull rate" means the mass of molten glass utilized in the manufacture of wool
fiberglass insulation at a single manufacturing line in a specified time
period.
(b) "Manufacturing line"
means the manufacturing equipment comprising the forming section, where molten
glass is fiberized and a fiberglass mat is formed; the curing section, where
the binder resin in the mat is thermally "set" ; and the cooling section, where
the mat is cooled.
(c) "Rotary
spin" means a process used to produce a wool fiberglass insulation by forcing
molten glass through numerous small orifices in the side wall of a spinner to
form continuous glass fibers that are then broken into discrete lengths by high
velocity air flow.
(d) "Wool
fiberglass insulation" means a thermal insulation material composed of glass
fibers and made from glass produced or melted at the same facility where the
manufacturing line is located.
(3) STANDARD FOR PARTICULATE MATTER. On and
after the date on which the performance test required to be conducted by s.
NR 440.18 is completed no owner or operator subject to
the provisions of this section may cause to be discharged into the atmosphere
from any affected facility any gases which contain particulate matter in excess
of 5.5 kg per Mg (11.0 lb/ton) of glass pulled.
(4) MONITORING OPERATIONS.
(a) Any owner or operator subject to the
provisions of this section who uses a wet scrubbing control device to comply
with the mass emission standard shall install, calibrate, maintain and operate
monitoring devices that measure the gas pressure drop across each scrubber and
the scrubbing liquid flow rate to each scrubber. The pressure drop monitor is
to be certified by its manufacturer to be accurate within plus or minus 250
pascals (" 1 inch water gauge) over its operating range and the flow rate
monitor is to be certified by its manufacturer to be accurate within "5% over
its operating range.
(b) An owner
or operator subject to the provisions of this section who uses a wet
electrostatic precipitator control device to comply with the mass emission
standard shall install, calibrate, maintain and operate monitoring devices that
measure the primary and secondary current (amperes) and voltage in each
electrical field and the inlet water flow rate. In addition the owner or
operator shall determine the total residue (total solids) content of the water
entering the control device once per day using Method 2450 B, "Total Solids
Dried at 103-105°C," in Standard Methods for the Examination of Water and
Wastewater, 20th edition, 1998, incorporated by reference in s.
NR 440.17(2) (e) 1. Total solids shall
be reported as percent by weight. All monitoring devices required under this
paragraph shall be certified by their manufacturers to be accurate within " 5%
over their operating range.
(c) All
monitoring devices required under this subsection are to be recalibrated
quarterly in accordance with procedures under s.
NR 440.13(2).
(5) RECORDKEEPING AND REPORTING REQUIREMENTS.
(a) At 30-minute intervals during each 2-hour
test run of each performance test of a wet scrubber control device, and at
least once every 4 hours thereafter, the owner or operator shall record the
measurements required by sub. (4) (a).
(b) At 30-minute intervals during each 2-hour
test run of each performance test of a wet electrostatic precipitator control
device, and at least once every 4 hours thereafter, the owner or operator shall
record the measurements required by sub. (4) (b), except that the concentration
of total residue in the water shall be recorded once during each performance
test and once per day thereafter.
(c) Records of the measurements required in
pars. (a) and (b) must be retained for at least 2 years.
(d) Each owner or operator shall submit
written semiannual reports of exceedances of control device operating
parameters required to be monitored by pars. (a) and (b) and written
documentation of, and a report of corrective maintenance required as a result
of, quarterly calibrations of the monitoring devices required in sub. (4) (c).
For the purpose of these reports exceedances are defined as any monitoring data
that are less than 70% of the lowest values or greater than 130% of the highest
value of each operating parameter recorded during the most recent performance
test.
(6) TEST METHODS
AND PROCEDURES.
(a) In conducting the
performance tests required in s.
NR 440.08, the
owner or operator shall use as reference methods and procedures the test
methods in Appendix A of 40 CFR part 60, incorporated by reference in s.
NR 440.17, or other methods and procedures as specified
in this subsection, except as provided in s.
NR 440.08(2).
(b) The owner or operator shall conduct
performance tests while the product with the highest loss on ignition (LOI)
expected to be produced by the affected facility is being
manufactured.
(c) The owner or
operator shall determine compliance with the particulate matter standard in
sub. (3) as follows:
1. The emission rate (E)
of particulate matter shall be computed for each run using the following
equation:
E =
(CtQsd)/(PavgK)
where:
E is the emission rate of particulate matter, kg/Mg
(lb/ton)
Ct is the concentration of particulate matter, g/dscm
(gr/dscf)
Qsd is the volumetric flow rate of effluent gas, dscm/hr
(dscf/hr)
Pavg is the average glass pull rate, Mg/hr (ton/hr)
K is the conversion factor, 1000 g/kg (7,000 gr/lb)
2. Method 5E shall be used to
determine the particulate matter concentration (Ct) and the volumetric flow
rate (Qsd) of the effluent gas. The sampling time and sample volume shall be at
least 120 minutes and 2.55 dscm (90.1 dscf).
3. The average glass pull rate (Pavg) for the
manufacturing line shall be the arithmetic average of 3 glass pull rate (Pi)
determinations taken at intervals of at least 30 minutes during each run.
The individual glass pull rates (Pi) shall be computed
using the following equation:
Pi =
K'LsWm[1.0-(LOI/100)]
where:
Pi is the glass pull rate at interval "i", Mg/hr
(ton/hr)
Ls is the line speed, m/min (Ft/min)
Wm is the trimmed mat width, m (ft)
M is the mat gram weight, g/m2 (lb/ft2)
LOI is the loss on ignition, weight percent
K' is the conversion factor, 6 10-5 (min-Mg)/(hr-g) [3 10-2
(min-ton)/(hr-lb)]
a. ASTM Standard
Test Method D2584-94, incorporated by reference in s.
NR 440.17(2) (a) 32., shall be used to
determine the LOI for each run.
b.
Line speed (Ls) trimmed mat width (Wm) and mat gram weight (M) shall be
determined for each run from the process information or from direct
measurements.
(d) To comply with sub. (5) (d), the owner or
operator shall record measurements as required in sub. (5) (a) and (b) using
the monitoring devices in sub. (4) (a) and (b) during the particulate matter
runs.