(a) Each owner or operator subject to the emission standard in Sec. 63.422(b) or 40 CFR 60.112b(a)(3)(ii) shall comply with the requirements in paragraphs (a)(1) and (2) of this section.
(1) Conduct a performance test on the vapor processing and collection systems according to either paragraph (a)(1)(i) or (ii) of this section.
(i) Use the test methods and procedures in 40 CFR 60.503 of this chapter, except a reading of 500 ppm shall be used to determine the level of leaks to be repaired under 40 CFR 60.503(b), or
(ii) Use alternative test methods and procedures in accordance with the alternative test method requirements in Sec. 63.7(f).
(2) The performance test requirements of 40 CFR 60.503(c) do not apply to flares defined in Sec. 63.421 and meeting the flare requirements in Sec. 63.11(b). The owner or operator shall demonstrate that the flare and associated vapor collection system is in compliance with the requirements in Sec. 63.11(b) and 40 CFR 60.503(a), (b), and (d), respectively.
(b) For each performance test conducted under paragraph (a) of this section, the owner or operator shall determine a monitored operating parameter value for the vapor processing system using the following procedure:
(1) During the performance test, continuously record the operating parameter under Sec. 63.427(a);
(2) Determine an operating parameter value based on the parameter data monitored during the performance test, supplemented by engineering assessments and the manufacturer's recommendations; and
(3) Provide for the Administrator's approval the rationale for the selected operating parameter value, and monitoring frequency and averaging time, including data and calculations used to develop the value and a description of why the value, monitoring frequency, and averaging time demonstrate continuous compliance with the emission standard in Sec. 63.422(b) or Sec. 60.112b(a)(3)(ii) of this chapter.
(c) For performance tests performed after the initial test, the owner or operator shall document the reasons for any change in the operating parameter value since the previous performance test.
(d) The owner or operator of each gasoline storage vessel subject to the provisions of Sec. 63.423 shall comply with Sec. 60.113b of this chapter. If a closed vent system and control device are used, as specified in Sec. 60.112b(a)(3) of this chapter, to comply with the requirements in Sec. 63.423, the owner or operator shall also comply with the requirements in paragraph (b) of this section.
(e) Annual certification test. The annual certification test for gasoline cargo tanks shall consist of the following test methods and procedures:
(1) Method 27, appendix A, 40 CFR part 60. Conduct the test using a time period (t) for the pressure and vacuum tests of 5 minutes. The initial pressure (Pi) for the pressure test shall be 460 mm H2 O (18 in. H2 O), gauge. The initial vacuum (Vi) for the vacuum test shall be 150 mm H2 O (6 in. H2 O), gauge. The maximum allowable pressure and vacuum changes ([Delta] p, [Delta] v) are as shown in the second column of Table 2 of this paragraph.
Table 2--Allowable Cargo Tank Test Pressure or Vacuum Change------------------------------------------------------------------------
Annual
certification-
allowable Allowable
pressure or pressure change
Cargo tank or compartment vacuum change ([Delta] p) in 5
capacity, liters (gal) ([Delta] p, minutes at any
[Delta] v) in 5 time, mm H2 O
minutes, mm H2 O (in. H2 O)
(in. H2 O)------------------------------------------------------------------------9,464 or more (2,500 or more)..... 25 (1.0) 64 (2.5)9,463 to 5,678 (2,499 to 1,500)... 38 (1.5) 76 (3.0)5,679 to 3,785 (1,499 to 1,000)... 51 (2.0) 89 (3.5)3,782 or less (999 or less)....... 64 (2.5) 102 (4.0)------------------------------------------------------------------------
(2) Pressure test of the cargo tank's internal vapor valve as follows:
(i) After completing the tests under paragraph (e)(1) of this section, use the procedures in Method 27 to repressurize the tank to 460 mm H2 O (18 in. H2 O), gauge. Close the tank's internal vapor valve(s), thereby isolating the vapor return line and manifold from the tank.
(ii) Relieve the pressure in the vapor return line to atmospheric pressure, then reseal the line. After 5 minutes, record the gauge pressure in the vapor return line and manifold. The maximum allowable 5-minute pressure increase is 130 mm H2 O (5 in. H2 O).
(f) Leak detection test. The leak detection test shall be performed using Method 21, appendix A, 40 CFR part 60, except omit section 4.3.2 of Method 21. A vapor-tight gasoline cargo tank shall have no leaks at any time when tested according to the procedures in this paragraph.
(1) The leak definition shall be 21,000 ppm as propane. Use propane to calibrate the instrument, setting the span at the leak definition. The response time to 90 percent of the final stable reading shall be less than 8 seconds for the detector with the sampling line and probe attached.
(2) In addition to the procedures in Method 21, include the following procedures:
(i) Perform the test on each compartment during loading of that compartment or while the compartment is still under pressure.
(ii) To eliminate a positive instrument drift, the dwell time for each leak detection shall not exceed two times the instrument response time. Purge the instrument with ambient air between each leak detection. The duration of the purge shall be in excess of two instrument response times.
(iii) Attempt to block the wind from the area being monitored. Record the highest detector reading and location for each leak.
(g) Nitrogen pressure decay field test. For those cargo tanks with manifolded product lines, this test procedure shall be conducted on each compartment.
(1) Record the cargo tank capacity. Upon completion of the loading operation, record the total volume loaded. Seal the cargo tank vapor collection system at the vapor coupler. The sealing apparatus shall have a pressure tap. Open the internal vapor valve(s) of the cargo tank and record the initial headspace pressure. Reduce or increase, as necessary, the initial headspace pressure to 460 mm H2 O (18.0 in. H2 O), gauge by releasing pressure or by adding commercial grade nitrogen gas from a high pressure cylinder capable of maintaining a pressure of 2,000 psig.
(i) The cylinder shall be equipped with a compatible two-stage regulator with a relief valve and a flow control metering valve. The flow rate of the nitrogen shall be no less than 2 cfm. The maximum allowable time to pressurize cargo tanks with headspace volumes of 1,000 gallons or less to the appropriate pressure is 4 minutes. For cargo tanks with a headspace of greater than 1,000 gallons, use as a maximum allowable time to pressurize 4 minutes or the result from the equation below, whichever is greater. T = Vh x 0.004 where: T = maximum allowable time to pressurize the cargo tank, min;Vh = cargo tank headspace volume during testing, gal.
(2) It is recommended that after the cargo tank headspace pressure reaches approximately 460 mm H2 O (18 in. H20), gauge, a fine adjust valve be used to adjust the headspace pressure to 460 mm H2 O (18.0 in. H2 O), gauge for the next 30 [5 seconds.
(3) Reseal the cargo tank vapor collection system and record the headspace pressure after 1 minute. The measured headspace pressure after 1 minute shall be greater than the minimum allowable final headspace pressure (PF) as calculated from the following equation:[GRAPHIC] [TIFF OMITTED] TR26JN95.000 where: (PF) = minimum allowable final headspace pressure, in.
H2 O, gauge;Vs = total cargo tank shell capacity, gal;Vh = cargo tank headspace volume after loading, gal;18.0 = initial pressure at start of test, in. H2 O, gauge;N = 5-minute continuous performance standard at any time from the third
column of Table 2 of Sec. 63.425(e)(i), inches H2
O.
(4) Conduct the internal vapor valve portion of this test by repressurizing the cargo tank headspace with nitrogen to 460 mm H2 O (18 in. H2 O), gauge. Close the internal vapor valve(s), wait for 30 [5 seconds, then relieve the pressure downstream of the vapor valve in the vapor collection system to atmospheric pressure. Wait 15 seconds, then reseal the vapor collection system. Measure and record the pressure every minute for 5 minutes. Within 5 seconds of the pressure measurement at the end of 5 minutes, open the vapor valve and record the headspace pressure as the ``final pressure.''
(5) If the decrease in pressure in the vapor collection system is less than at least one of the interval pressure change values in Table 3 of this paragraph, or if the final pressure is equal to or greater than 20 percent of the 1-minute final headspace pressure determined in the test in paragraph (g)(3) of this section, then the cargo tank is considered to be a vapor-tight gasoline cargo tank.
Table 3--Pressure Change for Internal Vapor Valve Test------------------------------------------------------------------------
Interval
pressure
Time interval change, mm
H2 O (in.
H2 O)------------------------------------------------------------------------After 1 minute............................................. 28 (1.1)After 2 minutes............................................ 56 (2.2)After 3 minutes............................................ 84 (3.3)After 4 minutes............................................ 112 (4.4)After 5 minutes............................................ 140 (5.5)------------------------------------------------------------------------
(h) Continuous performance pressure decay test. The continuous performance pressure decay test shall be performed using Method 27, appendix A, 40 CFR Part 60. Conduct only the positive pressure test using a time period (t) of 5 minutes. The initial pressure (Pi) shall be 460 mm H2 O (18 in. H2 O), gauge. The maximum allowable 5-minute pressure change ([Delta] p) which shall be met at any time is shown in the third column of Table 2 of Sec. 63.425(e)(1).
(i) Railcar bubble leak test procedures. As an alternative to paragraph (e) of this section for annual certification leakage testing of gasoline cargo tanks, the owner or operator may comply with paragraphs (i)(1) and (2) of this section for railcar gasoline cargo tanks, provided the railcar tank meets the requirement in paragraph (i)(3) of this section.
(1) Comply with the requirements of 49 CFR 173.31(d), 179.7, 180.509, and 180.511 for the testing of railcar gasoline cargo tanks.
(2) The leakage pressure test procedure required under 49 CFR 180.509(j) and used to show no indication of leakage under 49 CFR 180.511(f) shall be ASTM E 515-95 (incorporated by reference, see Sec. 63.14), BS EN 1593:1999 (incorporated by reference, see Sec. 63.14), or another bubble leak test procedure meeting the requirements in 49 CFR 179.7, 180.505, and 180.509.
(3) The alternative requirements in this paragraph (i) may not be used for any railcar gasoline cargo tank that collects gasoline vapors from a vapor balance system permitted under or required by a Federal, State, local, or tribal agency. A vapor balance system is a piping and collection system designed to collect gasoline vapors displaced from a storage vessel, barge, or other container being loaded, and routes the displaced gasoline vapors into the railcar gasoline cargo tank from which liquid gasoline is being unloaded. [59 FR 64318, Dec. 14, 1994; 60 FR 7627, Feb. 8, 1995; 60 FR 32913, June 26, 1995; 68 FR 70965, Dec. 19, 2003]