86.544-90—Calculations; exhaust emissions.
The final reported test results, with oxides of nitrogen being optional for model years prior to 2006 and required for 2006 and later model years, shall be computed by use of the following formula: (The results of all emission tests shall be rounded, in accordance with ASTM E29-93a (incorporated by reference in § 86.1 ), to the number of places to the right of the decimal point indicated by expressing the applicable standard to three significant figures.)
Where:
(1)
Ywm = Weighted mass emissions of CO2 Or of each pollutant (i.e., HC, CO, or NOX) in grams per vehicle kilometer and if appropriate, the weighted carbon mass equivalent of total hydrocarbon equivalent, in grams per vehicle kilometer.
(2)
Yct = Mass emissions as calculated from the “transient” phase of the cold-start test, in grams per test phase.
(3)
Yht = Mass emissions as calculated from the “transient” phase of the hot-start test, in grams per test phase.
(4)
Ys = Mass emissions as calculated from the “stabilized” phase of the cold-start test, in grams per test phase.
(5)
Dct = The measured driving distance from the “transient” phase of the cold-start test, in kilometers.
(6)
Dht = The measured driving distance from the “transient” phase of the hot-start test, in kilometers.
(7)
Ds = The measured driving distance from the “stabilized” phase of the cold-start test, in kilometers.
(b)
The mass of each pollutant for each phase of both the cold-start test and the hot-start test is determined from the following:
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(A)
For gasoline-fuel; DensityHC =576.8 g/m 3 -carbon atom (16.33 g/ft 3 -carbon atom), assuming an average carbon to hydrogen ratio of 1:1.85, at 20 °C (68 °F) and 101.3 kPa (760 mm Hg) pressure.
(B)
For natural gas and liquefied petroleum gas-fuel; DensityHC =41.57(12.011 H/C(1.008)) g/m 3 -carbon atom (1.1771(12.011 H/C(1.008)) g/ft 3 -carbon atom) where H/C is the hydrogen to carbon ratio of the hydrocarbon components of test fuel, at 20 °C (68 °F) and 101.3 kPa (760mm Hg) pressure.
(iii)
(A)
HCconc = Hydrocarbon concentration of the dilute exhaust sample corrected for background, in ppm carbon equivalent, i.e., equivalent propane×3.
Where:
(iv)
(A)
HCe = Hydrocarbon concentrations of the dilute exhaust sample as measured, in ppm carbon equivalent (propane ppm×3).
(v)
FID HCe =Concentration of hydrocarbon (plus methanol if methanol-fueled motorcycle is tested) in dilute exhaust as measured by the FID ppm carbon equivalent.
(vii)
CCH30He = Concentration of methanol in dilute exhaust as determined from the dilute exhaust methanol sample, ppm carbon.
(ix)
FID HCd =Concentration of hydrocarbon (plus methanol if methanol-fueled motorcycle is tested) in dilution air as measured by the FID, ppm carbon equivalent.
(x)
CCH3OHd = Concentration of methanol in dilution air as determined from dilution air methanol sample, ppm carbon.
(ii)
DensityN02 = Density of oxides of nitrogen in the exhaust gas, assuming they are in the form of nitrogen dioxide, 1913 g/m 3 (54.16 g/ft 3 ), at 20 °C (68 °F) and 101.3 kPa (760 mm Hg) pressure.
(iii)
(A)
NOxconc = Oxides of nitrogen concentration of the dilute exhaust sample corrected for background, ppm.
Where:
(ii)
DensityCO = Density of carbon monoxide, 1164 g/m 3 (32.97 g/ft 3 ), at 20 °C (68 °F) and 101.3 kPa (760 mm Hg) pressure.
(iii)
(A)
COconc = Carbon monoxide concentration of the dilute exhaust sample corrected for background, water vapor, and CO2 extraction, ppm.
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(iv)
(A)
COe = Carbon monoxide concentration of the dilute exhaust sample volume corrected for water vapor and carbon dioxide extraction, in ppm.
(B)
COe = (1 − 0.01925CO2e − 0.000323R)COem for gasoline-fueled vehicles with hydrogen to carbon ratio of 1.85:1
(C)
COe =[1 − (0.01 0.005HCR) CO2e − 0.000323R]COem for methanol-fueled, natural gas-fueled or liquefied petroleum gas-fueled motorcycles, where HCR is hydrogen to carbon ratio as measured for the fuel used.
(viii)
(A)
COd = Carbon monoxide concentration of the dilution air corrected for water vapor extraction, ppm.
Where:
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(ii)
DensityC02 = Density of carbon dioxide, 1830 g/m 3 (51.81 g/ft 3 ), at 20 °C (68 °F) and 101.3 kPa (760 mm Hg) pressure.
(iii)
(A)
CO2conc = carbon dioxide concentration of the dilute exhaust sample corrected for background, in percent.
Where:
(ii)
DensityCH3OH = Density of methanol is 1332 g/m 3 (37.71 g/ft 3 ), at 20 °C (68 °F) and 101.3 kPa (760 mm Hg) pressure.
Where:
(xiii)
AVs =Volume of absorbing reagent (deionized water) in impinger through which methanol sample from dilute exhaust is drawn, ml.
(xiv)
AVD =Volume of absorbing reagent (deionized water) in impinger through which methanol sample from dilution air is drawn, ml.
(ii)
DensityHCHO = Density of formaldehyde is 1249 g/m 3 (35.36 g/ft 3 ), at 20 °C (68 °F) and 101.3 kPa (760 mm Hg) pressure.
(iii)
(A)
HCHOconc = Formaldehyde concentration of the dilute exhaust corrected for background, ppm.
Where:
(vi)
CFDE = Concentration of DNPH derivative of formaldehyde from dilute exhaust sample in sampling solution, µg/ml.
(xii)
CFDA = Concentration of DNPH derivative of formaldehyde from dilution air sample in sampling solution, µg/ml.
(ii)
For methanol-fueled, natural gas-fueled or liquefied petroleum gas-fueled motorcycles, where fuel composition is Cx Hy Oz as measured, or calculated, for the fuel used (for natural gas and liquefied petroleum gas-fuel, Z=0):
(iii)
(A)
Vmix = Total dilute exhaust volume in cubic meters per test phase corrected to standard conditions (293 °K (528 °R) and 101.3 kPa (760 mm Hg)).
Where:
(iv)
Vo = Volume of gas pumped by the positive displacement pump, in cubic meters per revolution. This volume is dependent on the pressure differential across the positive displacement pump. (See calibration techniques in § 86.519.)
(v)
N = Number of revolutions of the positive displacement pump during the test phase while samples are being collected.
(vii)
Pi = Pressure depression below atmospheric measured at the inlet to the positive displacement pump, kPa.
(viii)
Tp = Average temperature of dilute exhaust entering positive displacement pump during test while samples are being collected, °K.
Where:
(d)
Sample calculation of mass emission values for gasoline-fueled vehicles with engine displacements equal to or greater than 170 cc (10.4 cu. in.):
(1)
For the “transient” phase of the cold-start test, assume Vo = 0.0077934 m 3 per rev; N = 12,115; R = 20.5 pct; Ra = 20.5 pct; PB = 99.05 kPa; Pd = 3.382 kPa; Pi = 9.851 kPa; Tp = 309.8 °K; HCe = 249.75 ppm carbon equivalent; NOxe = 38.30 ppm; COem = 311.23 ppm; CO2e = 0.415 percent; HCd = 4.90 ppm; NOxd = 0.30 ppm; COdm = 8.13 ppm; CO2d = 0.037 pct; Dct = 5.650 km.
Then:
(i)
Vmix = [(0.0077934)(12,115)(99.05-9.851)(293.15)]/ [(101.325)(309.8)] = 78.651 m 3 per test phase.
(2)
For the “stabilized” portion of the cold-start test, assume that similar calculations resulted in HCmass = 7.184 grams per test phase; NOxmass = 2.154 grams per test phase; COmass = 64.541 grams per test phase; and CO2mass = 529.52 grams per test phase. Ds = 6.070 km.
(3)
For the “transient” portion of the hot-start test, assume that similar calculations resulted in HCmass = 6.122 grams per test phase; NOxmass = 7.056 grams per test phase; COmass = 34.964 grams per test phase; and CO2mass = 480.93 grams per test phase. Dht = 5.660 km.
(4)
For a 1978 motorcycle with an engine displacement equal to or greater than 170 cc (10.4 cu. in):
(i)
HCwm = 0.43 [(11.114 7.184)/(5.650 6.070)] 0.57 [(6.122 7.184)/(5.660 6.070)] = 1.318 grams per vehicle kilometer.
(ii)
NOxwm = 0.43 [(4.733 = 2.154)/(5.650 = 6.070)] = 0.57 [(7.056 = 2.154)/(5.660 = 6.070)] = 0.700 gram per vehicle kilometer.
(iii)
COwm = 0.43 [(27.362 64.541)/(5.650 6.070)] 0.57 [(34.964 64.541)/(5.660 6.070)] = 8.207 grams per vehicle kilometer.
(iv)
CO2wm = 0.43 [(549.81 529.52)/(5.650 6.070)] 0.57 [(480.93 529.52)/(5.660 6.070)] = 88.701 grams per vehicle kilometer.