NR 440.35(7)(b)2.
2. The continuous monitoring system of
sub. (6) (a) 2. shall be used to determine the SO
2 concentrations on a dry basis. The sampling time for each run shall be 2 hours, and the average SO
2 concentration for the 2-hour period shall be computed as in
sub. (6) (b). The monitoring system drift during the run may not exceed 2% of the span value.
NR 440.35 History
History: Cr.
Register, January, 1984, No. 337, eff. 2-1-84; am. (2) (intro.),
Register, September, 1990, No. 417, eff. 10-1-90; am. (6) (a) 2. a. and b., r. and recr. (7),
Register, July, 1993, No. 451, eff. 8-1-9
3; am. (6) (a) 2. b.,
Register, December, 1995, No. 480, eff. 1-1-96.
NR 440.36
NR 440.36 Primary aluminum reduction plants. NR 440.36(1)(1)
Applicability and designation of affected facility. NR 440.36(1)(a)(a) The affected facilities in primary aluminum reduction plants to which this section applies are potroom groups and anode bake plants.
NR 440.36(1)(b)
(b) Except as provided in
par. (c), any affected facility under
par. (a) that commences construction or modification after October 23, 1974, is subject to the requirements of this section.
NR 440.36(1)(c)
(c) An owner or operator of an affected facility under
par. (a) may elect to comply with the requirements of this section or the requirements of
40 CFR part 63.
NR 440.36(2)
(2) Definitions. As used in this section, terms not defined in this subsection have the meanings given in
s. NR 440.02.
NR 440.36(2)(a)
(a) “Aluminum equivalent" means an amount of aluminum which can be produced from a Mg of anodes produced by an anode bake plant as determined by
sub. (6) (b) 4. b.
NR 440.36(2)(b)
(b) “Anode bake plant" means a facility which produces carbon anodes for use in a primary aluminum reduction plant.
NR 440.36(2)(c)
(c) “Potroom" means a building unit which houses a group of electrolytic cells in which aluminum is produced.
NR 440.36(2)(d)
(d) “Potroom group" means an uncontrolled potroom, a potroom which is controlled individually, or a group of potrooms or potroom segments ducted to a common control system.
NR 440.36(2)(e)
(e) “Primary aluminum reduction plant" means any facility manufacturing aluminum by electrolytic reduction.
NR 440.36(2)(f)
(f) “Primary control system" means an air pollution control system designed to remove gaseous and particulate fluorides from exhaust gases which are captured at the cell.
NR 440.36(2)(g)
(g) “Roof monitor" means that portion of the roof of a potroom where gases not captured at the cell exit from the potroom.
NR 440.36(2)(h)
(h) “Total fluorides" means elemental fluorine and all fluoride compounds as measured by reference methods specified in
sub. (6) or by equivalent or alternative methods.
NR 440.36(3)(a)(a) On and after the date on which the initial performance test required to be conducted by
s. NR 440.08 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 containing total fluorides, as measured according to
sub. (6), in excess of:
NR 440.36(3)(a)1.
1. 1.0 kg/Mg (2.0 lb/ton) of aluminum produced for potroom groups at Soderberg plants, except that emissions between 1.0 kg/Mg and 1.3 kg/Mg (2.6 lb/ton) shall be considered in compliance if the owner or operator demonstrates that exemplary operation and maintenance procedures were used with respect to the emission control system and that proper control equipment was operating at the affected facility during the performance tests;
NR 440.36(3)(a)2.
2. 0.95 kg/Mg (1.9 lb/ton) of aluminum produced for potroom groups at prebake plants, except that emissions between 0.95 kg/Mg and 1.25 kg/Mg (2.5 lb/ton) shall be considered in compliance if the owner or operator demonstrates that exemplary operation and maintenance procedures were used with respect to the emission control system and that proper control equipment was operating at the affected facility during the performance test; and
NR 440.36(3)(a)3.
3. 0.050 kg/Mg (0.10 lb/ton) of aluminum equivalent for anode bake plants.
NR 440.36(3)(b)
(b) Within 30 days of any performance test which reveals emissions which fall between the 1.0 kg/Mg and 1.3 kg/Mg levels in
par. (a) 1. or between to 0.95 kg/Mg and 1.25 kg/Mg levels in
par. (a) 2., the owner or operator shall submit a report to the department indicating whether all necessary control devices were on-line and operating properly during the performance test, describing the operating and maintenance procedures followed, and setting forth any explanation for the excess emissions.
NR 440.36(4)(a)(a) On and after the date on which the performance test required to be conducted by
s. NR 440.08 is completed, no owner or operator subject to the provisions of this section may cause to be discharged into the atmosphere:
NR 440.36(4)(a)1.
1. From any potroom group any gases which exhibit 10% opacity or greater, or
NR 440.36(4)(a)2.
2. From any anode bake plant any gases which exhibit 20% opacity or greater.
NR 440.36(5)(a)(a) The owner or operator of any affected facility subject to the provisions of this section shall install, calibrate, maintain and operate monitoring devices which can be used to determine daily the weight of aluminum and anode produced. The weighing devices shall have an accuracy of
" 5% over their operating range.
NR 440.36(5)(b)
(b) The owner or operator of any affected facility shall maintain a record of daily production rates of aluminum and anodes, raw material feed rates, and cell or potline voltages.
NR 440.36(5)(c)
(c) Following the initial performance test as required under
s. NR 440.08 (1), an owner or operator shall conduct a performance test at least once each month during the life of the affected facility, except when malfunctions prevent representative sampling, as provided under
s. NR 440.08 (3). The owner or operator shall give the department at least 15 days advance notice of each test. The department may require additional testing under
ch. NR 439.
NR 440.36 Note
Note:
Under
40 CFR 60.195 (b), an owner or operator may petition the administrator to establish an alternate testing requirement that requires testing less frequently than once each month for a primary control system or an anode bake plant if it can be shown that their emissions have low variability during day-to-day operations. The alternative testing requirement must be published in the federal register and include a testing schedule and, in the case of a primary control system, the method to be used to determine primary control system emissions for the purpose of performance tests.
NR 440.36(6)(a)(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).
NR 440.36(6)(b)
(b) The owner or operator shall determine compliance with the total fluorides and visible emission standards in
subs. (3) and
(4) as follows:
NR 440.36(6)(b)1.
1. The emission rate (E
p) of total fluorides from potroom groups shall be computed for each run using the following equation:
Ep = [(Cs Qsd)1 + (Cs Qsd)2]/(PK)
where:
Ep is the emission rate of total fluorides from a potroom group, kg/Mg (lb/ton)
Cs is the concentration of total fluorides, mg/dscm (gr/dscf)
Qsd is the volumetric flow rate of effluent gas, dscm/hr (dscf/hr)
P is the aluminum production rate, Mg/hr (ton/hr)
K is the conversion factor, 106 mg/kg (7000 gr/lb)
1 is the subscript for primary control system effluent gas
2 is the subscript for secondary control system or roof monitor effluent gas
NR 440.36(6)(b)2.
2. The emission rate (E
b) of total fluorides from anode bake plants shall be computed for each run using the following equation:
Eb = (Cs Qsd)/(PeK)
where:
Eb is the emission rate of total fluorides, kg/Mg (lb/ton) of aluminum equivalent
Cs is the concentration of total fluorides, mg/dscm (gr/dscf)
Qsd is the volumetric flow rate of effluent gas, dscm/hr (dscf/hr)
Pe is the aluminum equivalent for anode production rate, Mg/hr (ton/hr)
K is the conversion factor, 106 mg/kg (7000 gr/lb)
NR 440.36(6)(b)3.
3. Method 13A or 13B shall be used for ducts or stacks and Method 14 for roof monitors not employing stacks or pollutant collection systems, to determine the total fluorides concentration (C
s) and volumetric flow rate (Q
sd) of the effluent gas. The sampling time and sample volume for each run shall be at least 8 hours and 6.80 dscm (240 dscf) for potroom groups and at least 4 hours and 3.40 dscm (120 dscf) for anode bake plants.
NR 440.36(6)(b)4.
4. The monitoring devices of
sub. (5) (a) shall be used to determine the daily weight of aluminum and anode produced.
NR 440.36(6)(b)4.a.
a. The aluminum production rate (P) shall be determined by dividing 720 hours into the weight of aluminum tapped from the affected facility during a period of 30 days before and including the final run of a performance test.
NR 440.36(6)(b)4.b.
b. The aluminum equivalent production rate (P
e) for anodes shall be determined as 2 times the average weight of anode produced during a representative oven cycle divided by the cycle time. An owner or operator may establish a multiplication factor other than 2 by submitting production records of the amount of aluminum produced and the concurrent weight of anodes consumed by the potrooms.
NR 440.36 History
History: Cr.
Register, January, 1984, No. 337, eff. 2-1-84; am. (6) (a),
Register, September, 1986, No. 369, eff. 10-1-86; am. (2) (intro.), (3) (a) 3., (6) (a), r. (6) (b),
Register, September, 1990, No. 417, eff. 10-1-90; renum. (6) (a)to be (5) (c), cr. (6) (a) and (b), r. (6) (c) to (i),
Register, July, 1993, No. 451, eff. 8-1-93
; correction in (2) (a) made under s. 13.93 (2m) (b) 7., Stats.,
Register, November, 1999, No. 527;
CR 06-109: am. (1) (b), (3) (a) (intro.) and (6) (b) 1. and 2., cr. (1) (c) Register May 2008 No. 629, eff. 6-1-08. NR 440.37
NR 440.37 Phosphate fertilizer industry: wet-process phosphoric acid plants. NR 440.37(1)
(1)
Applicability and designation of affected facility. NR 440.37(1)(a)(a) The affected facility to which the provisions of this section apply is each wet-process phosphoric acid plant having a design capacity of more than 15 tons of equivalent P
2O
5 feed per calendar day. For the purpose of this section, the affected facility includes any combination of: reactors, filters, evaporators and hotwells.
NR 440.37(1)(b)
(b) Any facility under
par. (a) that commences construction or modification after October 22, 1974, is subject to the requirements of this section.
NR 440.37(2)
(2) Definitions. As used in this section, terms not defined in this subsection have the meanings given in
s. NR 440.02.
NR 440.37(2)(a)
(a) “Equivalent P
2O
5 feed" means the quantity of phosphorus, expressed as phosphorus pentoxide, fed to the process.
NR 440.37(2)(b)
(b) “Total fluorides" means elemental fluorine and all fluoride compounds as measured by reference methods specified in
sub. (5), or equivalent or alternative methods.
NR 440.37(2)(c)
(c) ``Wet-process phosphoric acid plant" means any facility manufacturing phosphoric acid by reacting phosphate rock and acid.
NR 440.37(3)
(3) Standard for fluorides. On and after the date on which the performance test required to be conducted by
s. NR 440.08 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 to which contain total fluorides in excess of 10.0 g/Mg of equivalent P
2O
5 feed (0.020 lb/ton).
NR 440.37(4)(a)(a) The owner or operator of any wet-process phosphoric acid plant subject to the provisions of this section shall install, calibrate, maintain and operate a monitoring device which can be used to determine the mass flow of phosphorous-bearing feed material to the process. The monitoring device shall have an accuracy of
$5% over its operating range.
NR 440.37(4)(b)
(b) The owner or operator of any wet-process phosphoric acid plant shall maintain a daily record of equivalent P
2O
5 feed by first determining the total mass rate in Mg/hr of phosphorus bearing feed using a monitoring device for measuring mass flow rate which meets the requirements of
par. (a) and then by proceeding according to
sub. (5) (b) 3.
NR 440.37(4)(c)
(c) The owner or operator of any wet-process phosphoric acid plant subject to the provisions of this section shall install, calibrate, maintain and operate a monitoring device which continuously measures and permanently records the total pressure drop across the process scrubbing system. The monitoring device shall have an accuracy of
" 5% over its operating range.
NR 440.37(5)(a)(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).
NR 440.37(5)(b)
(b) The owner or operator shall determine compliance with the total fluorides standard in
sub. (3) as follows:
where:
E is the emission rate of total fluorides, g/Mg (lb/ton) of equivalent P2O5 feed
Csi is the concentration of total fluorides from emission point “i", mg/dscm (gr/dscf)
Qsdi is the volumetric flow rate of effluent gas from emission point “i", dscm/hr (dscf/hr)
N is the number of emission points associated with the affected facility
P is the equivalent P2O5 feed rate, Mg/hr (ton/hr)
K is the conversion factor, 1000 mg/g (7000 gr/lb)
NR 440.37(5)(b)2.
2. Method 13A or 13B shall be used to determine the total fluorides concentration (C
si) and volumetric flow rate (Q
sdi ) of the effluent gas from each of the emission points. The sampling shall be at least 60 minutes and 0.85 dscm (30 dscf).
NR 440.37(5)(b)3.
3. The equivalent P
2O
5 feed rate (P) shall be computed for each run using the following equation:
P = Mp Rp
where:
Mp is the total mass flow rate of phosphorus-bearing feed, Mg/hr (ton/hr)
Rp is the P2O5 content, decimal fraction
