Title 40
PART 86 APPENDIX III
Parameter | Symbol | Units | Tolerance |
---|---|---|---|
Barometric pressure (corrected) | PB | “Hg | ±.01 “Hg. |
Ambient temperature | TA | °F | ±.5 °F. |
Air Temperature into LFE | ETI | °F | ±.1 °F. |
Pressure depression upstream of LFE | EPI | “H20 | ±.1“H20. |
Pressure drop across the LFE matrix | EDP | “H20 | ±.005“H20. |
Air temperature at CVS pump inlet | PTI | °F | ±.5 °F. |
Pressure depression at CVS pump inlet | PPI | “Fluid | ±.05“Fluid. |
Specific gravity of manometer fluid | Sp. Gr. | ||
Pressure head at CVS pump outlet | PPO | “Fluid | ±.05“Fluid. |
Air temperature at CVS pump outlet (optional) | PTO | °F | ±.5 °F. |
Pump revolutions during test period | N | Revs | None. |
Elapsed time for test period | t | Seconds | ±.05 Seconds. |
Note: The fluid level in the manometer tube should stabilize before the reading is made and the elapsed time for revolution counting should be greater than 120 seconds.
Reset the restrictor valve to a more restricted condition in an increment of pump inlet depression (about 4″ H2O) that will yield a minimum of six data points for the total calibration.
Allow the system to stabilize for 3 minutes and repeat the data acquisition.
Data Analysis:The data recorded during the calibration are to be used in the following calculations.
1. The air flow rate at each test point is calculated in standard cubic feet per minute (Qs) from the flowmeter data using the manufacturer's prescribed method.
2. The air flow rate is then converted to pump flow, Vo, in cubic feet per revolution at absolute pump inlet temperature and pressure.
Vo = Qs/n × Tp/530 × 29.92/Pp where: Qs = Meter air flow rate in standard cubic feet per minute (flowmeter standard conditions are 70 °F, 29.92 “Hg). n = Pump speed in revolutions per minute. Pp = Absolute pump inlet pressure, in (“Hg). Pp = PB-PPI (SP.GR./13.57), Tp = PTI + 460.3. The correlation function at each test point is then calculated from the calibration data, as follows:
ΔPp = The pressure differential from pump inlet to pump outlet in (“Hg). ΔPp = Pe−Pp Pe = Absolute pump outlet pressure, in (“Hg). Pp = PB + PPO (Sp. Gr./13.57)See § 86.177-22 for other definitions.
4. A linear least squares fit is performed to generate the calibration equations which have the forms
Vo = Do−M(Xo) n = A−B(Pp)Do, M, A, and B are the slope-intercept constants describing the lines.
A CVS system that has multiple speeds should be calibrated on each speed used. The calibration curves generated for the ranges will be approximately parallel and the intercept values, Do, will increase as the pump flow range decreases.
If the calibration has been performed carefully, the calculated Vo values from the equation will be within ±.50% of the measured value of Vo. Values of M will vary from one pump to another, but values of Do for pumps of the same make, model, and range should agree within ±3 percent of each other. Particulate influx from use will cause the pump slip to decrease as reflected by lower values for M. Calibrations should be performed at 0, 30, 100, 200, 400, etc. hours of pump operation to assure the stability of the pump slip rate. Analysis of mass injection data will also reflect pump slip stability.
CVS System Verification:The following technique can be used to verify that the CVS and analytical instruments can accurately measure a mass of gas that has been injected into the system.
1. Obtain a small cylinder that has been charged with pure propane or carbon monoxide gas (caution - carbon monoxide is poisonous!). Critical flow orifice devices can also be used for constant flow metering.
2. Determine a reference cylinder weight to the nearest 0.01 gram.
3. Operate the CVS in the normal manner and release a quantity of pure propane or carbon monoxide into the system during the sampling period.
4. The calculations of § 86.177-22 are performed in a normal way except, in the case of propane, the density of propane (17.30 grams/cu./ft./carbon atom) is used in place of the density of exhaust hydrocarbons. In the case of carbon monoxide, the density of 32.97 grams/cu. ft. is used.
5. The gravimetric mass is subtracted from the CVS measured mass and then divided by the gravimetric mass to determine the percent accuracy of the system.
6. The cause for any discrepancy greater than ±2 percent should be found and corrected. The following list of parametric errors may assist the operator in locating the cause of large errors.
Positive Error (Indication is higher than true value):
1. Calculated Vo is greater than actual Vo.
a. Original calibration in error.
2. Pump inlet temperature recorder is reading low. A 6 °F. discrepancy will give a 1 percent error.
3. Pump inlet pressure indicator is reading high. A 3.5 in. H2O high reading will give 1 percent error.
4. Background concentration reading is too low. Check analyzer zero. Check leakage at floor inlet.
5. Analyzer is reading high. Check span.
6. Barometer reading is in error (too high). Barometric pressure reading should be gravity and temperature corrected.
7. Revolution counter is reading high (Check pump speed and counters.)
8. Mixture is stratified causing the sample to be higher than the average concentration in the mixture. Negative Error (Indication is lower than true value):
1. Calculated Vo is less than actual Vo.
a. Original calibration in error.
b. Pump clearances decreased due to influx of some surface adherent material. Recalibration may be needed.
2. Pump inlet temperature recorder is reading high.
3. Pump inlet pressure indicator is reading low.
4. Background concentration reading is too high.
5. Analyzer is reading low.
6. Barometer reading is in error (too low).
7. Revolution counter is reading low.
8. There is a leak into the sampling system. Pressure check the lines and fittings on the intake side of sample transfer pumps on both the CVS and analyzer console.
[42 FR 33000, June 28, 1977]