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.
NR 440.29(1)(b)(b) Any facility under par. (a) that commences construction or modification after June 11, 1973, is subject to the requirements of this section.
NR 440.29(2)(2)Definitions. As used in this section, terms not defined in this subsection have the meanings given in s. NR 440.02.
NR 440.29(2)(a)(a) “Blast furnace” means any furnace used to recover metal from slag.
NR 440.29(2)(b)(b) “Lead” means elemental lead or alloys in which the predominant component is lead.
NR 440.29(2)(c)(c) “Reverberatory furnace” includes the following types of reverberatory furnaces: stationary, rotating, rocking and tilting.
NR 440.29(2)(d)(d) “Secondary lead smelter” means any facility producing lead from a leadbearing scrap material by smelting to the metallic form.
NR 440.29(3)(3)Standard for particulate matter.