NR 440.285(6)(d)1.1. A report containing the measurements required by s. NR 440.18 (6) shall be furnished to the department as required by s. NR 440.08. This report shall be submitted within 6 months of the initial startup date.
NR 440.285(6)(d)2.2. Records shall be kept of all periods of operation during which the flare pilot flame is absent.
NR 440.285(6)(d)3.3. Semiannual reports of all periods recorded under subd. 2. in which the pilot flame was absent shall be furnished to the department.
NR 440.285(7)(7)Monitoring of operations.
NR 440.285(7)(a)(a) The owner or operator shall keep copies of all records required by this section, except for the record required by par. (b) for at least 2 years. The record required by par. (b) shall be kept for the life of the source.
NR 440.285(7)(b)(b) The owner or operator of each storage vessel as specified in sub. (1) (a) shall keep readily accessible records showing the dimensions of the storage vessel and an analysis showing the capacity of the storage vessel.
NR 440.285(7)(c)(c) Except as provided in pars. (f) and (g), the owner or operator of each storage vessel either with a design capacity greater than or equal to 151 m3 storing a liquid with a maximum true vapor pressure greater than or equal to 3.6 kPa, or with a design capacity greater than or equal to 75 m3 but less than 151 m3 storing a liquid with a maximum true vapor pressure greater than or equal to 15.0 kPa, shall maintain a record of the VOL stored, the period of storage, and the maximum true vapor pressure of that VOL during the respective storage period.
NR 440.285(7)(d)(d) Except as provided in par. (g), the owner or operator of each storage vessel either with a design capacity greater than or equal to 151 m3 storing a liquid with a maximum true vapor pressure that is normally less than 5.2 kPa, or with a design capacity greater than or equal to 75 m3 but less than 151 m3 storing a liquid with a maximum true vapor pressure that is normally less than 27.6 kPa, shall notify the department within 30 days when the maximum true vapor pressure of the liquid exceeds the respective maximum true vapor pressure values for each volume range.
NR 440.285(7)(e)(e) Available data on the storage temperature may be used to determine the maximum true vapor pressure as follows:
NR 440.285(7)(e)1.1. For vessels operated above or below ambient temperatures, the maximum true vapor pressure is calculated based upon the highest expected calendar-month average of the storage temperature. For vessels operated at ambient temperatures, the maximum true vapor pressure is calculated based upon the maximum local monthly average ambient temperature as reported by the national weather service.
NR 440.285(7)(e)2.2. For crude oil or refined petroleum products the vapor pressure may be obtained by the following:
NR 440.285(7)(e)2.a.a. Available data on the Reid vapor pressure and the maximum expected storage temperature based on the highest expected calendar-month average temperature of the stored product may be used to determine the maximum true vapor pressure from nomographs contained in API Publication 2517, incorporated by reference in s. NR 440.17, unless the department specifically requests that the liquid be sampled, the actual storage temperature determined, and the Reid vapor pressure determined from the sample or samples.
NR 440.285(7)(e)2.b.b. The true vapor pressure of each type of crude oil with a Reid vapor pressure less than 13.8 kPa or with physical properties that preclude determination by the recommended method is to be determined from available data and recorded if the estimated maximum true vapor pressure is greater than 3.5 kPa.
NR 440.285(7)(e)3.3. For other liquids, the vapor pressure may be obtained from one of the following:
NR 440.285(7)(e)3.a.a. Standard reference texts.
NR 440.285(7)(e)3.b.b. Use of ASTM Method D2879-97, incorporated by reference in s. NR 440.17 (2) (a) 34.
NR 440.285(7)(e)3.c.c. Measurement by an appropriate method approved by the administrator.
NR 440.285(7)(e)3.d.d. Calculation using an appropriate method approved by the administrator.
NR 440.285(7)(f)(f) The owner or operator of each vessel storing a waste mixture of indeterminate or variable composition shall be subject to the following requirements.
NR 440.285(7)(f)1.1. Prior to the initial filling of the vessel, the highest maximum true vapor pressure for the range of anticipated liquid compositions to be stored shall be determined using the methods described in par. (e).
NR 440.285(7)(f)2.2. For vessels in which the vapor pressure of the anticipated liquid composition is above the cutoff for monitoring but below the cutoff for controls as defined in sub. (3) (a), an initial physical test of the vapor pressure is required; and a physical test at least once every 6 months thereafter is required as determined by one of the following methods:
NR 440.285(7)(f)2.a.a. ASTM D2879-97, incorporated by reference in s. NR 440.17 (2) (a).
NR 440.285(7)(f)2.b.b. ASTM D323-94 incorporated by reference in s. NR 440.17 (2) (a) 11.
NR 440.285(7)(f)2.c.c. Measurement by an appropriate method as approved by the administrator.
NR 440.285(7)(g)(g) The owner or operator of each vessel equipped with a closed vent system and control device meeting the specifications of sub. (3) or with emissions reductions equipment as specified in 40 CFR 65.42 (b) (4), (b) (5), (b) (6) or (c) as in effect on December 14, 2000 is exempt from the requirements of pars. (c) and (d).
NR 440.285 HistoryHistory: Cr. Register, September, 1990, No. 417, eff. 10-1-90; am (1) (c), (2) (f) (intro.) and (4) (a) 4., Register, July, 1993, No. 451, eff. 8-1-93; am. (2) (f) 1., (7) (e) 2. a., Register, December, 1995, No. 480, eff. 1-1-96; am., Register, November, 1999, No. 527, eff. 12-1-99; CR 06-109: am. (1) (a) and (b), (2) (f), (i), (j) (intro.) and 1. and (k), (7) (b), (e) 3., (f) 2. and (g), r. (1) (c), cr. (1) (d) 8. and (e), (2) (hm) and (j) 3. Register May 2008 No. 629, eff. 6-1-08; corrections in (1) (e) 2. and (4) (c) 1. (intro.) made under s. 13.92 (4) (b) 7., Stats., Register May 2008 No. 629.
NR 440.29NR 440.29Secondary lead smelters.
NR 440.29(1)(1)Applicability and designations of affected facility.
NR 440.29(1)(a)(a) The provisions of this section are applicable to the following affected facilities in secondary lead smelters: pot furnaces of more than 250 kg (550 lb) charging capacity, blast (cupola) furnaces and reverberatory furnaces.