NR 440.27(4)(b)(b) Available data on the typical Reid vapor pressure and the maximum expected storage 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 one or more samples. NR 440.27(4)(c)(c) The true vapor pressure of each type of crude oil with a Reid vapor pressure less than 13.8 kPa (2.0 psia) or whose physical properties preclude determination by the recommended method is to be determined from available data and recorded if the estimated true vapor pressure is greater than 6.9 kPa (1.0 psia). NR 440.27(4)(d)(d) The following are exempt from the requirements of this subsection: NR 440.27(4)(d)1.1. Each owner or operator of each affected facility which stores petroleum liquids with a Reid vapor pressure of less than 6.9 kPa (1.0 psia) provided the maximum true vapor pressure does not exceed 6.9 kPa (1.0 psia). NR 440.27(4)(d)2.2. Each owner or operator of each affected facility equipped with a vapor recovery and return or disposal system in accordance with the requirements of sub. (3). NR 440.27 HistoryHistory: Cr. Register, January, 1984, No. 337, eff. 2-1-84; am. (2) (intro.) and (i), Register, September, 1990, No. 417, eff. 10-1-90; am. (2) (k) and (4) (b), Register, July, 1993, No. 451, eff. 8-1-93; CR 06-109: am. (2) (g) and (i) Register May 2008 No. 629, eff. 6-1-08. NR 440.28NR 440.28 Storage vessels for petroleum liquids for which construction, reconstruction or modification commenced after May 18, 1978, and prior to July 23, 1984. NR 440.28(1)(1) Applicability and designation of affected facility. NR 440.28(1)(a)(a) Except as provided in par. (b), the affected facility to which this section applies is each storage vessel with a storage capacity greater than 151,416 liters (40,000 gallons) that is used to store petroleum liquids for which construction is commenced after May 18, 1978. NR 440.28(1)(b)(b) Each petroleum liquid storage vessel with a capacity of less than 1,589,873 liters (420,000 gallons) used for petroleum or condensate stored, processed, or treated prior to custody transfer is not an affected facility and, therefore, is exempt from the requirements of this section. NR 440.28(1)(c)1.1. Owners or operators may choose to comply with 40 CFR part 65, subpart C, as in effect on December 14, 2000, to satisfy the requirements of subs. (3) to (5) for storage vessels that are subject to this section that store petroleum liquies that, as stored, have a maximum true vapor pressure equal to or greater than 10.3 kPa (1.5 psia). Other provisions applying to owners or operators who choose to comply with 40 CFR part 65 are provided in 40 CFR 65.1. NR 440.28(1)(c)2.2. Owners or operators who choose to comply with 40 CFR part 65, subpart C, as in effect on December 14, 2000, shall also comply with ss. NR 440.01, 440.02, 440.05, 440.06, 440.07 (1) (a) and (d), 440.14 and 440.15 for those storage vessels. Any section or subsection from ss. NR 440.01 to 440.19 not specified in this subdivision does not apply to owners or operators of storage vessels complying with 40 CFR part 65, subpart C, except that provisions required to be met prior to implementing 40 CFR part 65 still apply. Owners and operators who choose to comply with 40 CFR part 65, subpart C, shall comply with 40 CFR part 65, subpart A, as in effect on December 14, 2000. NR 440.28(2)(2) Definitions. As used in this section, terms not defined in this subsection have the meanings given in s. NR 440.02. NR 440.28(2)(a)(a) “Condensate” means hydrocarbon liquid separated from natural gas which condenses due to changes in the temperature or pressure, or both, and remains liquid at standard conditions. NR 440.28(2)(b)(b) “Custody transfer” means the transfer of produced petroleum or condensate, or both, after processing or treating, or both, in the producing operations, from storage tanks or automatic transfer facilities to pipelines or any other forms of transportation. NR 440.28(2)(c)(c) “Liquid-mounted seal” means a foam or liquid-filled primary seal mounted in contact with the liquid between the tank wall and the floating roof continuously around the circumference of the tank. NR 440.28(2)(d)(d) “Metallic shoe seal” includes but is not limited to a metal sheet held vertically against the tank wall by springs or weighted levers and is connected by braces to the floating roof. A flexible coated fabric (envelope) spans the annular space between the metal sheet and the floating roof. NR 440.28(2)(e)(e) “Petroleum” means the crude oil removed from the earth and the oils derived from tar sands, shale and coal. NR 440.28(2)(f)(f) “Petroleum liquids” means petroleum, condensate, and any finished or intermediate products manufactured in a petroleum refinery but does not mean Nos. 2 through 6 fuel oils as specified in ASTM D396-98, gas turbine fuel oils Nos. 2-GT through 4-GT as specified in ASTM D2880-96, or diesel fuel oils Nos. 2-D and 4-D as specified in ASTM D975-98a. These 3 ASTM methods are incorporated by reference in s. NR 440.17 (2) (a) 13., 36. and 14., respectively. NR 440.28(2)(g)(g) “Petroleum refinery” means each facility engaged in producing gasoline, kerosene, distillate fuel oils, residual fuel oils, lubricants, or other products through distillation of petroleum or through redistillation, cracking, extracting or reforming of unfinished petroleum derivatives. NR 440.28(2)(h)(h) “Reid vapor pressure” is the absolute vapor pressure of volatile crude oil and volatile nonviscous petroleum liquids, except liquified petroleum gases, as determined by ASTM D323-94, incorporated by reference in s. NR 440.17 (2) (a) 11. NR 440.28(2)(i)(i) “Storage vessel” means each tank, reservoir or container used for the storage of petroleum liquids, but does not include: NR 440.28(2)(i)1.1. Pressure vessels which are designed to operate in excess of 204.9 kPa (15 psig) without emissions to the atmosphere except under emergency conditions. NR 440.28(2)(i)3.3. Underground tanks if the total volume of petroleum liquids added to and taken from the tank annually does not exceed twice the volume of the tank. NR 440.28(2)(j)(j) “True vapor pressure” means the equilibrium partial pressure exerted by a petroleum liquid such as determined in accordance with methods described in American Petroleum Institute Publication 2517, Evaporation Loss from External Floating Roof Tanks, Second Edition, February 1980, incorporated by reference in s. NR 440.17. NR 440.28(2)(k)(k) “Vapor-mounted seal” means a foam-filled primary seal mounted continuously around the circumference of the tank so there is an annular vapor space underneath the seal. The annular vapor space is bounded by the bottom of the primary seal, the tank wall, the liquid surface, and the floating roof. NR 440.28(3)(3) Standard for volatile organic compounds (VOC).