['Air Programs']
['Air Emissions']
03/21/2023
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(a) Overview. This section describes how to calibrate flow meters for diluted exhaust constant-volume sampling (CVS) systems. We recommend that you also use this section to calibrate flow meters that use a subsonic venturi or ultrasonic flow to measure raw exhaust flow. You may follow the molar flow calibration procedures in 40 CFR 1065.340 instead of the procedures in this section.
(b) Scope and frequency. Perform this calibration while the flow meter is installed in its permanent position, except as allowed in paragraph (c) of this section. Perform this calibration after you change any part of the flow configuration upstream or downstream of the flow meter that may affect the flow-meter calibration. Perform this calibration upon initial CVS installation and whenever corrective action does not resolve a failure to meet the diluted exhaust flow verification (i.e., propane check) in 40 CFR 1065.341.
(c) Ex-situ CFV and SSV calibration. You may remove a CFV or SSV from its permanent position for calibration as long as the flow meter meets the requirements in 40 CFR 1065.340(c).
(d) Reference flow meter. Calibrate each CVS flow meter using a reference flow meter such as a subsonic venturi flow meter, a long-radius ASME/NIST flow nozzle, a smooth approach orifice, a laminar flow element, or an ultrasonic flow meter. Use a reference flow meter that reports quantities that are NIST-traceable within ±1% uncertainty. Use this reference flow meter's response to flow as the reference value for CVS flow-meter calibration.
(e) Configuration. Calibrate the system with any upstream screens or other restrictions that will be used during testing and that could affect the flow ahead of the flow meter. You may not use any upstream screen or other restriction that could affect the flow ahead of the reference flow meter, unless the flow meter has been calibrated with such a restriction.
(f) PDP calibration. Calibrate each positive-displacement pump (PDP) to determine a flow-versus-PDP speed equation that accounts for flow leakage across sealing surfaces in the PDP as a function of PDP inlet pressure. Determine unique equation coefficients for each speed at which you operate the PDP. Calibrate a PDP flow meter as follows:
(1) Connect the system as shown in Figure 1 of this section.
(2) Leaks between the calibration flow meter and the PDP must be less than 0.3% of the total flow at the lowest calibrated flow point; for example, at the highest restriction and lowest PDP-speed point.
(3) While the PDP operates, maintain a constant temperature at the PDP inlet within ±2% of the mean absolute inlet temperature, T ͞/>in.
(4) Set the PDP speed to the first speed point at which you intend to calibrate.
(5) Set the variable restrictor to its wide-open position.
(6) Operate the PDP for at least 3 min to stabilize the system. Continue operating the PDP and record the mean values of at least 30 seconds of sampled data of each of the following quantities:
(i) The mean flow rate of the reference flow meter, V ̇̅/>ref. This may include several measurements of different quantities, such as reference meter pressures and temperatures, for calculating V ̇̅/>ref.
(ii) The mean temperature at the PDP inlet, T ͞/>in.
(iii) The mean static absolute pressure at the PDP inlet, P ͞/>in.
(iv) The mean static absolute pressure at the PDP outlet, P ͞/>out.
(v) The mean PDP speed, f ͞/>nPDP.
(7) Incrementally close the restrictor valve to decrease the absolute pressure at the inlet to the PDP, Pin.
(8) Repeat the steps in paragraphs (f)(6) and (7) of this section to record data at a minimum of six restrictor positions ranging from the wide-open restrictor position to the minimum expected pressure at the PDP inlet or the maximum expected differential (outlet minus inlet) pressure across the PDP during testing.
(9) Calibrate the PDP by using the collected data and the equations in §1066.625(a).
(10) Repeat the steps in paragraphs (f)(6) through (9) of this section for each speed at which you operate the PDP.
(11) Use the equations in §1066.630(a) to determine the PDP flow equation for emission testing.
(12) Verify the calibration by performing a CVS verification (i.e., propane check) as described in 40 CFR 1065.341.
(13) During emission testing ensure that the PDP is not operated either below the lowest inlet pressure point or above the highest differential pressure point in the calibration data.
(g) SSV calibration. Calibrate each subsonic venturi (SSV) to determine its discharge coefficient, Cd, for the expected range of inlet pressures. Calibrate an SSV flow meter as follows:
(1) Configure your calibration system as shown in Figure 1 of this section.
(2) Verify that any leaks between the calibration flow meter and the SSV are less than 0.3% of the total flow at the highest restriction.
(3) Start the blower downstream of the SSV.
(4) While the SSV operates, maintain a constant temperature at the SSV inlet within ±2% of the mean absolute inlet temperature, T ͞/>in.
(5) Set the variable restrictor or variable-speed blower to a flow rate greater than the greatest flow rate expected during testing. You may not extrapolate flow rates beyond calibrated values, so we recommend that you make sure the Reynolds number, Re#, at the SSV throat at the greatest calibrated flow rate is greater than the maximum Re# expected during testing.
(6) Operate the SSV for at least 3 min to stabilize the system. Continue operating the SSV and record the mean of at least 30 seconds of sampled data of each of the following quantities:
(i) The mean flow rate of the reference flow meter, V ̇̅/>ref. This may include several measurements of different quantities for calculating V ̇̅/>ref, such as reference meter pressures and temperatures.
(ii) The mean temperature at the venturi inlet, T ͞/>in.
(iii) The mean static absolute pressure at the venturi inlet, p ͞/>in.
(iv) Mean static differential pressure between the static pressure at the venturi inlet and the static pressure at the venturi throat, Δp ͞/>ssv.
(7) Incrementally close the restrictor valve or decrease the blower speed to decrease the flow rate.
(8) Repeat the steps in paragraphs (g)(6) and (7) of this section to record data at a minimum of ten flow rates.
(9) Determine an equation to quantify Cd as a function of Re# by using the collected data and the equations in §1066.625(b). Section 1066.625 also includes statistical criteria for validating the Cd versus Re# equation.
(10) Verify the calibration by performing a CVS verification (i.e., propane check) as described in 40 CFR 1065.341 using the new Cd versus Re# equation.
(11) Use the SSV only between the minimum and maximum calibrated Re#. If you want to use the SSV at a lower or higher Re#, you must recalibrate the SSV.
(12) Use the equations in §1066.630(b) to determine SSV flow during a test.
(h) CFV calibration. The calibration procedure described in this paragraph (h) establishes the value of the calibration coefficient, Kv, at measured values of pressure, temperature and air flow. Calibrate the CFV up to the highest expected pressure ratio, r, according to §1066.625. Calibrate the CFV as follows:
(1) Configure your calibration system as shown in Figure 1 of this section.
(2) Verify that any leaks between the calibration flow meter and the CFV are less than 0.3% of the total flow at the highest restriction.
(3) Start the blower downstream of the CFV.
(4) While the CFV operates, maintain a constant temperature at the CFV inlet within ±2% of the mean absolute inlet temperature, T ͞/>in.
(5) Set the variable restrictor to its wide-open position. Instead of a variable restrictor, you may alternately vary the pressure downstream of the CFV by varying blower speed or by introducing a controlled leak. Note that some blowers have limitations on nonloaded conditions.
(6) Operate the CFV for at least 3 min to stabilize the system. Continue operating the CFV and record the mean values of at least 30 seconds of sampled data of each of the following quantities:
(i) The mean flow rate of the reference flow meter, V ̇̅/>ref. This may include several measurements of different quantities, such as reference meter pressures and temperatures, for calculating V ̇̅/>ref.
(ii) The mean temperature at the venturi inlet, T ͞/>in.
(iii) The mean static absolute pressure at the venturi inlet, p ͞/>in.
(iv) The mean static differential pressure between the CFV inlet and the CFV outlet, Δp ͞/>CFV.
(7) Incrementally close the restrictor valve or decrease the downstream pressure to decrease the differential pressure across the CFV, ΔpCFV.
(8) Repeat the steps in paragraphs (h)(6) and (7) of this section to record mean data at a minimum of ten restrictor positions, such that you test the fullest practical range of Δp ͞/>CFV expected during testing. We do not require that you remove calibration components or CVS components to calibrate at the lowest possible restriction.
(9) Determine Kv and the highest allowable pressure ratio, r, according to §1066.625.
(10) Use Kv to determine CFV flow during an emission test. Do not use the CFV above the highest allowed r, as determined in §1066.625.
(11) Verify the calibration by performing a CVS verification (i.e., propane check) as described in 40 CFR 1065.341.
(12) If your CVS is configured to operate multiple CFVs in parallel, calibrate your CVS using one of the following methods:
(i) Calibrate every combination of CFVs according to this section and §1066.625(c). Refer to §1066.630(c) for instructions on calculating flow rates for this option.
(ii) Calibrate each CFV according to this section and §1066.625. Refer to §1066.630 for instructions on calculating flow rates for this option.
(i) Ultrasonic flow meter calibration. [Reserved]
[79 FR 23823, Apr. 28, 2014, as amended at 81 FR 74197, Oct. 25, 2016]
['Air Programs']
['Air Emissions']