NOTICE

This technical report does not necessarily represent final EPA decisions or 

positions. It is intended to present technical analysis of issues using data 

that are currently available. The purpose in the release of such reports is to 

facilitate the exchange of technical information and to inform the public of 

technical developments.

Assessment and Standards Division

Office of Transportation and Air Quality

U.S. Environmental Protection Agency

National Renewable Energy Laboratory

U.S. Department of Energy

Coordinating Research Council

EPAct/V2/E-89: Assessing the Effect 

of Five Gasoline Properties on Exhaust 

Emissions from Light-Duty Vehicles 

Certified to Tier 2 Standards

Final Report on Program Design and 

Data Collection

Appendix E

Spreadsheets of Detailed 

Round Robin Fuel Inspection Data

EPA-420-R-13-004

April 2013
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 1 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7208 0.7212 - 0.7213 0.7211 - - - - - - - - - 0.7211

API Gravity, 60oF

o

API D4052 64.6 64.5 - 64.5 64.6 - - - - - - - - - 64.6

Ethanol vol. % D5599 - - 11.46 10.21 - - - 9.59 - - - 10.13 10.09 10.14 10.03

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 - - <0.10

Distillation IBP oF 92.6 91.9 - - - 93.0 - - 93.0 92.3 94.6 - - 93.8 92.9

5% evap oF 112.0 112.7 - - - 111.6 - - 111.9 112.4 113.6 - - 112.5 112.5

10% evap oF 117.2 117.6 - - - 116.7 - - 116.7 117.1 118.0 - - 117.2 117.3

20% evap oF 124.0 124.1 - - - 120.0 - - 123.4 124.0 124.1 - - 123.9 123.9

30% evap oF 130.8 131.6 - - - 130.9 - - 130.8 131.3 131.5 - - 130.9 131.2

40% evap oF 139.9 140.1 - - - 139.5 - - 139.5 139.8 140.0 - - 139.5 139.9

50% evap oF 148.8 149.4 - - - 148.7 - - 148.1 149.3 149.1 - - 148.6 148.9

60% evap oF 172.0 171.2 - - - 170.5 - - 171.8 173.9 172.7 - - 177.3 172.3

70% evap oF 223.9 223.3 - - - 223.9 - - 224.2 225.0 224.3 - - 225.7 224.1

80% evap oF 254.7 253.1 - - - 252.8 - - 254.5 255.5 255.2 - - 256.0 254.6

90% evap oF 300.0 300.7 - - - 298.5 - - 299.6 300.3 300.5 - - 302.5 300.2

95% evap oF 334.2 334.6 - - - 333.6 - - 334.1 334.6 335.1 - - 338.0 334.5

FBP oF 367.8 368.0 - - - 366.3 - - 366.3 365.1 372.6 - - 367.7 368.0

Recovery vol. % 98.4 98.2 - - - 98.5 - - 97.8 98.5 98.4 - - 98.4 98.4

Residue vol. % 1.0 1.1 - - - 1.0 - - 1.1 1.0 1.0 - - 1.1 1.0

Loss vol. % 0.6 0.7 - - - 0.5 - - 1.1 0.5 0.6 - - 0.5 0.6

Corrected Recovery vol. % 98.4 98.2 - - - - - - - 98.5 98.4 - - - 98.4

Corrected Loss vol. % 0.6 0.7 - - - - - - - 0.5 0.6 - - - 0.6

DVPE (EPA equation) psi D5191 10.11 10.16 10.02 10.11 9.28 10.09 - 10.00 - - 10.05 9.88 - 10.05 10.07

Aromatics vol. % D1319 - 15.8 - 15.0 15.4 16.2 - 15.8 - - - - 14.2 15.5 15.4

Olefins vol. % D1319 - 8.5 - 7.7 8.0 7.2 - 6.5 - - - - 7.7 7.5 7.6

Saturates vol. % * - - - - - - - - - - - - - - 67.0

Benzene vol. % D3606 - - - 0.64 - - - 0.59 - - - 0.62 0.56 0.71 0.62

S mg/kg D5453 29 33 28 28 - - - 32 - - - - - 30 30

RON - D2699 94.7 - 94.9 - - - - 94.8 - - - - - 94.9 94.8

MON - D2700 85.4 - 85.8 - - - - 87.3 - - - - - 86.7 86.3

(RON+MON)/2 - - 90.1 - 90.4 - - - - 91.1 - - - - - 90.8 90.6

C mass % D5291 mod.** 82.40 - - - 80.50 - - - - - - - 81.72 82.16 81.70

H mass % D5291 mod.** 14.01 - - - 14.12 - - - - - - - 14.36 13.60 14.02

O mass % D5599 - - 4.4 3.9 - - - 3.7 - - - 3.9 3.9 3.9 3.9

Net Heat of Combustion MJ/kg D4809 42.042 - - - - - - 41.848 - - - - - 41.958 41.950

Water mass % E-1064 - - - - - - - 0.052 - - - 0.089 - - 0.0705

Lead g/l D3237 - - - - - - - - - - - - - - -

Copper Strip Corrosion - D130 - - - - - - - 1A - - - - - - 1A

Solvent Washed Gum 

Content mg/100ml D381 - - - - - - - <0.5 - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - - >240 - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

PROPERTY UNIT

Laboratory

Average TEST 

METHOD
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 2 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7217 0.7221 - 0.7222 0.7221 - - - - - - - - - 0.7220

API Gravity, 60oF

o

API D4052 64.3 64.3 - 64.2 64.3 - - - - - - - - - 64.3

Ethanol vol. % D5599 - - - - - - <0.01 - - - - <0.10 <0.05 <0.10 <0.10

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 - <0.10 <0.10

Distillation IBP oF 75.6 80.0 91.6 86.1 85.3 79.3 82 - - 80.9 85.4 85.8 87.4 83 83.5

5% evap oF 106.2 106.0 112.1 104.6 103.1 99.2 97 - - 104.8 105.5 106.1 115.6 105 105.4

10% evap oF 122.5 122.4 126.3 119.4 120.2 116.4 117 - - 121.5 121.3 122.0 130.8 121 121.7

20% evap oF 156.4 155.9 156.9 151.0 151.5 150.9 152 - - 154.7 153.0 153.9 163.0 153 154.4

30% evap oF 192.2 192.1 191.3 188.0 187.5 189.0 190 - - 191.1 189.3 189.9 197.2 190 190.6

40% evap oF 218.9 219.6 219.0 216.9 216.7 217.8 218 - - 218.8 217.7 217.9 222.2 218 218.5

50% evap oF 237.0 237.6 237.7 235.1 235.2 236.6 237 - - 236.9 236.4 236.0 238.9 236 236.7

60% evap oF 252.6 253.2 253.2 254.5 250.0 251.8 253 - - 252.5 252.0 251.8 257.0 251 252.7

70% evap oF 271.4 271.9 272.7 270.4 270.1 271.0 271 - - 271.7 271.4 271.2 275.8 272 271.7

80% evap oF 305.8 305.7 305.6 304.0 305.1 304.6 306 - - 304.7 305.4 305.0 313.4 305 305.9

90% evap oF 340.0 340.7 341.2 339.7 339.4 337.5 342 - - 337.2 337.4 340.6 344.0 341 340.1

95% evap oF 351.8 352.5 353.8 351.6 352.2 351.0 356 - - 351.1 350.9 352.1 359.5 353 353.0

FBP oF 374.7 376.3 376.3 370.0 375.8 375.2 373 - - 371.3 377.8 380.8 377.9 375 375.3

Recovery vol. % 97.9 97.1 97.5 97 96.2 97.3 97 - - 97.1 96.5 97.1 97.4 96.8 97.2

Residue vol. % 1.1 1.1 1.0 0.5 1.3 1.1 1.2 - - 1.1 1.0 0.9 1.2 0.9 1.0

Loss vol. % 1.0 1.8 1.3 2.5 2.6 1.6 1.8 - - 1.8 2.5 2.0 1.4 2.3 1.8

Corrected Recovery vol. % 98 97.2 97.7 97.7 - - - - - 97.1 97.2 97.5 97.3 - 97.5

Corrected Loss vol. % 0.9 1.7 1.5 1.8 - - - - - 1.8 1.8 1.6 1.5 - 1.6

DVPE (EPA equation) psi D5191 10.14 10.28 10.01 10.30 9.43 10.08 10.25 - - - 10.20 10.14 - 10.38 10.20

Aromatics vol. % D1319 - 13.8 - 13.7 14.1 14.2 14.1 - - - - - 14.4 14.1 14.1

Olefins vol. % D1319 - 7.2 - 6.8 7.8 6.3 5.7 - - - - - 6.9 7.2 6.8

Saturates vol. % * - - - - - - - - - - - - - - 79.1

Benzene vol. % D3606 - - - 0.55 - - 0.46 - - - - 0.52 - 0.50 0.51

S mg/kg D5453 22 26 22 22 - - 25 - - - - - - 23 23

RON - D2699 96.0 - 96.2 - - - 96.1 - - - - - - 95.7 96.0

MON - D2700 88.3 - 88.7 - - - 88.4 - - - - - - 89.1 88.6

(RON+MON)/2 - - 92.2 - 92.5 - - - 92.3 - - - - - - 92.4 92.3

C mass % D5291 mod.** 84.88 - - - 84.77 - - - - - - - 85.44 85.39 85.12

H mass % D5291 mod.** 14.22 - - - 14.63 - - - - - - - 14.61 14.25 14.43

O mass % D5599 - - - - - - <0.1 - - - - <0.1 <0.01 - <0.1

Net Heat of Combustion MJ/kg D4809 44.320 - - - - - 43.600 - - - - - - 43.960 43.960

Water mass % E-1064 - - - - - - 0.005 - - - - 0.014 - - 0.0095

Lead g/l D3237 - - - - - - <0.001 - - - - - - - <0.001

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 3 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7347 0.7351 - 0.7350 0.7350 - - - - - - - - - 0.7350

API Gravity, 60oF

o

API D4052 60.8 60.8 - 60.8 60.8 - - - - - - - - - 60.8

Ethanol vol. % D5599 - - 11.44 10.47 - - 10.15 - - - - 10.38 10.36 10.42 10.36

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 - - <0.10

Distillation IBP oF 104.6 104.6 - - - 106.7 - - - 107.4 105.9 - - 109.2 106.4

5% evap oF 135.5 136.3 - - - 135.6 - - - 135.6 136.2 - - 137.0 136.0

10% evap oF 141.6 141.6 - - - 141.4 - - - 141.6 141.4 - - 142.3 141.7

20% evap oF 149.1 149.4 - - - 148.7 - - - 148.9 148.6 - - 148.6 148.9

30% evap oF 155.3 155.3 - - - 154.7 - - - 154.8 154.9 - - 155.1 155.0

40% evap oF 174.5 174.3 - - - 174.8 - - - 175.3 171.8 - - 180.1 175.1

50% evap oF 217.4 218.5 - - - 216.8 - - - 217.3 216.8 - - 218.3 217.5

60% evap oF 231.7 230.9 - - - 231.1 - - - 231.1 231.5 - - 224.6 230.2

70% evap oF 243.5 244.9 - - - 242.9 - - - 242.1 243.3 - - 244.6 243.6

80% evap oF 258.1 259.6 - - - 247.7 - - - 259.4 257.1 - - 260.4 257.1

90% evap oF 295.5 295.7 - - - 293.7 - - - 296.8 293.2 - - 300.3 295.9

95% evap oF 334.4 332.9 - - - 332.7 - - - 334.1 332.0 - - 340.2 334.4

FBP oF 372.2 370.2 - - - 366.4 - - - 368.5 364.5 - - 371.8 368.9

Recovery vol. % 98.6 98.6 - - - 98.9 - - - 98.4 98.0 - - 98.2 98.4

Residue vol. % 1.0 1.0 - - - 1.0 - - - 1.1 1.0 - - 1.0 1.0

Loss vol. % 0.4 0.4 - - - 0.1 - - - 0.5 1.0 - - 0.8 0.6

Corrected Recovery vol. % 98.6 98.6 - - - - - - - 98.4 98.1 - - - 98.4

Corrected Loss vol. % 0.4 0.4 - - - - - - - 0.5 0.9 - - - 0.6

DVPE (EPA equation) psi D5191 6.99 7.04 6.85 7.04 6.33 - 6.89 - - - 6.99 6.88 - 6.78 6.93

Aromatics vol. % D1319 - 15.1 - 14.6 14.3 15.7 - 14.6 - - - - 15.0 15.9 15.0

Olefins vol. % D1319 - 8.1 - 7.5 7.5 7.8 - 6.8 - - - - 8.0 7.3 7.6

Saturates vol. % * - - - - - - - - - - - - - - 67.0

Benzene vol. % D3606 - - - 0.58 - - 0.54 - - - - 0.57 0.63 0.75 0.61

S mg/kg D5453 20 23 19 21 - - 23 - - - - - - 26 22

RON - D2699 98.1 - 98.3 - - - 97.7 - - - - - - 97.8 98.0

MON - D2700 87.6 - 88.2 - - - 86.9 - - - - - - 87.6 87.6

(RON+MON)/2 - - 92.9 - 93.3 - - - 92.3 - - - - - - 92.7 92.8

C mass % D5291 mod.** 81.69 - - - 80.50 - - - - - - - 81.80 82.44 81.61

H mass % D5291 mod.** 14.13 - - - 14.12 - - - - - - - 14.39 14.04 14.17

O mass % D5599 - - 4.3 3.9 - - 3.8 - - - - 3.9 3.9 3.9 3.9

Net Heat of Combustion MJ/kg D4809 41.996 - - - - - 40.860 - - - - - - 41.750 41.536

Water mass % E-1064 - - - - - - 0.051 - - - - 0.067 - - 0.059

Lead g/l D3237 - - - - - - - - - - - - - - -

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 4 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7343 0.7349 - 0.7347 0.7346 - - - - - - - - - 0.7346

API Gravity, 60oF

o

API D4052 60.9 60.8 - 60.9 60.9 - - - - - - - - - 60.9

Ethanol vol. % D5599 - - 10.74 9.96 - - - - 10.02 - - 10.05 9.85 9.83 9.94

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 0.06 - <0.10

Distillation IBP oF 87.9 90.8 - - - 90.7 - - 87.8 89.3 91.7 - - 90.8 89.9

5% evap oF 114.8 115.2 - - - 112.8 - - 118.6 114.5 117.4 - - 118.0 115.9

10% evap oF 125.4 126.1 - - - 124.0 - - 127.9 125.2 128.1 - - 127.1 126.3

20% evap oF 140.6 140.8 - - - 139.0 - - 141.9 140.3 142.3 - - 141.3 140.9

30% evap oF 151.7 151.8 - - - 150.6 - - 152.4 151.2 152.4 - - 152.1 151.7

40% evap oF 158.9 162.3 - - - 157.8 - - 162.9 160.7 160.4 - - 165.1 161.2

50% evap oF 220.2 220.5 - - - 218.6 - - 225.1 220.9 224.2 - - 223.8 221.9

60% evap oF 245.1 246.2 - - - 239.2 - - 248.2 246.5 248.0 - - 247.9 245.9

70% evap oF 269.5 270.1 - - - 266.5 - - 272.4 269.0 269.9 - - 272.3 270.0

80% evap oF 302.2 302.3 - - - 301.8 - - 308.3 300.8 302.5 - - 306.6 303.5

90% evap oF 336.5 335.7 - - - 336.2 - - 340.5 336.5 337.3 - - 339.8 337.5

95% evap oF 350.6 351.0 - - - 350.4 - - 355.2 350.3 350.7 - - 355.7 352.0

FBP oF 370.5 370.8 - - - 368.8 - - 368.7 368.0 371.1 - - 370.7 369.8

Recovery vol. % 97.5 97.3 - - - 97.0 - - 97.3 97.5 97.2 - - 97.5 97.4

Residue vol. % 1.1 1.1 - - - 1.1 - - 1.1 1.1 1.1 - - 1.0 1.1

Loss vol. % 1.4 1.6 - - - 1.9 - - 1.6 1.4 1.7 - - 1.5 1.5

Corrected Recovery vol. % 97.7 97.3 - - - - - - - 97.4 97.5 - - - 97.5

Corrected Loss vol. % 1.2 1.6 - - - - - - - 1.5 1.4 - - - 1.4

DVPE (EPA equation) psi D5191 10.03 10.11 9.70 10.11 9.28 10.03 10.10 - 10.05 - 9.32 9.93 - 10.00 10.01

Aromatics vol. % D1319 - 15.7 - 15.7 15.6 16.0 - - 15.1 - - - 14.7 15.6 15.5

Olefins vol. % D1319 - 7.4 - 6.4 8.0 6.1 - - 6.1 - - - 6.7 6.9 6.8

Saturates vol. % * - - - - - - - - - - - - - - 67.8

Benzene vol. % D3606 - - - 0.54 - - - - 0.51 - - 0.52 0.57 0.57 0.54

S mg/kg D5453 20 24 19 20 - - - - 30 - - - - 21 21

RON - D2699 96.9 - 97.3 - - - 97.2 - - - - - - 97.1 97.1

MON - D2700 87.0 - 87.8 - - - 87.5 - - - - - - 87.9 87.6

(RON+MON)/2 - - 92.0 - 92.6 - - - 92.4 - - - - - - 92.5 92.4

C mass % D5291 mod.** 82.18 - - - 81.35 - - - - - - - 82.21 82.23 82.21

H mass % D5291 mod.** 14.18 - - - 14.11 - - - - - - - 14.27 13.90 14.12

O mass % D5599 - - 4.0 3.7 - - - - 3.8 - - 3.8 3.7 3.7 3.7

Net Heat of Combustion MJ/kg D4809 42.256 - - - - - 41.678 - - - - - - 41.924 41.952

Water mass % E-1064 - - - - - - - - 0.063 - - 0.090 - - 0.077

Lead g/l D3237 - - - - - - - - - - - - - - -

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - 1.5 - - - - - - - 1.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 5 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7571 0.7575 - 0.7574 0.7573 - - - - - - - - - 0.7573

API Gravity, 60oF

o

API D4052 55.2 55.1 - 55.1 55.2 - - - - - - - - - 55.2

Ethanol vol. % D5599 - - - - - - <0.10 - - - - <0.10 <0.05 <0.10 <0.10

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 - - <0.10

Distillation IBP oF 91.3 92.6 100.4 93.9 99.7 93.5 - - 89.9 92.0 92.3 95.1 94.8 94 94.1

5% evap oF 127.2 129.8 134.6 122.4 127.6 126.7 - - 125.3 129.2 131.2 128.7 135.3 125 128.6

10% evap oF 144.7 146.8 149.4 140.1 145.2 143.5 - - 142.4 145.9 147.4 145.5 150.5 143 145.4

20% evap oF 172.8 174.3 175.1 168.2 171.9 170.3 - - 170.4 173.9 174.2 172.7 176.4 171 172.6

30% evap oF 199.9 200.9 200.1 196.6 198.3 198.2 - - 197.7 200.5 200.8 199.6 202.3 198 199.4

40% evap oF 222.0 223.6 222.3 221.6 221 221.2 - - 220.3 223.4 222.5 222.7 223.3 221 222.1

50% evap oF 237.0 238.0 237.2 237.0 236.1 236.4 - - 235.4 237.7 237.2 237.8 237.9 236 237.0

60% evap oF 247.6 248.2 248.0 241.1 246.9 247.2 - - 247.2 248.2 247.9 247.8 248.1 248 247.2

70% evap oF 258.6 258.6 258.3 258.5 257.5 258.0 - - 257.8 258.5 258.4 258.5 258.7 260 258.5

80% evap oF 273.3 273.8 273.6 272.6 272.1 272.3 - - 271.8 273.3 273.1 273.2 274.0 274 273.1

90% evap oF 300.9 300.6 301.1 298.0 298.8 298.1 - - 299.7 300.7 300.4 299.7 300.6 301 300.0

95% evap oF 324.3 323.4 325.2 320.5 321.6 323.1 - - 322.0 325.5 323.8 323.8 324.5 324 323.5

FBP oF 357.2 358.9 356.4 351.3 358.7 356.6 - - 354.3 363.5 360.5 358.2 358.5 360 357.8

Recovery vol. % 98.0 98.0 98.8 97.2 98 98.1 - - 98.5 98.4 98.3 98.1 98.7 97.3 98.2

Residue vol. % 1.0 1.0 0.8 0.6 1.1 1.0 - - 1.0 1.0 1.0 0.8 1.0 1.0 0.9

Loss vol. % 1.0 1.0 0.4 2.2 0.9 0.9 - - 0.5 0.6 0.7 1.1 0.3 1.7 0.9

Corrected Recovery vol. % 98.1 98.0 98.8 97.8 - - - - - 98.4 98.3 98.3 98.7 - 98.3

Corrected Loss vol. % 0.9 1.0 0.4 1.6 - - - - - 0.6 0.7 0.9 0.3 - 0.8

DVPE (EPA equation) psi D5191 6.98 7.04 6.90 7.01 6.34 6.89 7.05 - - - 6.99 6.85 - 6.86 6.95

Aromatics vol. % D1319 - 35.2 - 35.6 33.4 34.8 - 34.0 - - - - 34.3 35.8 34.7

Olefins vol. % D1319 - 7.4 - 6.2 7.3 7.1 - 5.7 - - - - 7.5 7.0 6.9

Saturates vol. % * - - - - - - - - - - - - - - 58.4

Benzene vol. % D3606 - - - 0.55 - - 0.48 - - - - 0.52 - 0.49 0.51

S mg/kg D5453 22 27 22 24 - - 26 - - - - - - 25 24

RON - D2699 96.6 - 96.6 - - - 97.2 - - - - - - 96.2 96.7

MON - D2700 86.2 - 86.6 - - - 86.1 - - - - - - 86.4 86.3

(RON+MON)/2 - - 91.4 - 91.6 - - - 91.7 - - - - - - 91.3 91.5

C mass % D5291 mod.** 86.25 - - - 86.08 - - - - - - - 86.99 86.98 86.58

H mass % D5291 mod.** 12.70 - - - 12.92 - - - - - - - 13.02 13.04 12.92

O mass % D5599 - - - - - - <0.1 - - - - <0.1 <0.01 - <0.1

Net Heat of Combustion MJ/kg D4809 43.260 - - - - - 42.672 - - - - - - 42.914 42.948

Water mass % E-1064 - - - - - - 0.004 - - - - 0.024 - - 0.014

Lead g/l D3237 - - - - - - <0.003 - - - - - - - <0.003

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 6 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7340 0.7343 - 0.7342 0.7341 - - - - - - - - - 0.7342

API Gravity, 60oF

o

API D4052 61.0 61.0 - 61.1 61.1 - - - - - - - - - 61.1

Ethanol vol. % D5599 - - 11.74 10.66 - - 9.97 - - - - 10.58 10.44 10.55 10.56

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - 0.01 - - - - <0.10 0.06 - <0.10

Distillation IBP oF 105.6 106.3 - - - 106.1 - - 106.4 106.9 106.6 - - 108.8 106.7

5% evap oF 129.8 130.7 - - - 129.3 - - 130.7 130.7 129.5 - - 131.9 130.4

10% evap oF 135.8 136.3 - - - 135.0 - - 135.7 136.4 135.4 - - 136.7 135.9

20% evap oF 142.7 143.0 - - - 141.9 - - 142.4 143.1 142.3 - - 143.1 142.6

30% evap oF 148.4 148.7 - - - 147.5 - - 147.9 148.8 147.9 - - 148.6 148.3

40% evap oF 153.9 153.4 - - - 152.7 - - 153.0 154.2 152.6 - - 154.1 153.4

50% evap oF 186.7 187.9 - - - 185.6 - - 189.4 189.3 185.1 - - 195.7 188.5

60% evap oF 227.4 228.0 - - - 225.3 - - 230.3 229.1 226.7 - - 230.8 228.2

70% evap oF 265.6 266.9 - - - 264.8 - - 270.7 266.9 265.3 - - 273.7 267.7

80% evap oF 308.8 309.6 - - - 306.8 - - 313.2 310.2 307.3 - - 314.9 310.1

90% evap oF 340.1 340.1 - - - 338.7 - - 342.2 340.5 336.9 - - 344.3 340.4

95% evap oF 351.5 351.4 - - - 350.6 - - 354.5 352.2 350.5 - - 358.0 352.7

FBP oF 370.8 371.3 - - - 367.4 - - 370.1 363.8 371.2 - - 369.9 369.2

Recovery vol. % 98 97.7 - - - 98.3 - - 97.6 98.0 97.5 - - 97.1 97.8

Residue vol. % 1.0 1.0 - - - 1.0 - - 1.0 1.0 1.0 - - 1.1 1.0

Loss vol. % 1.0 1.3 - - - 0.7 - - 1.4 1.0 1.5 - - 1.8 1.2

Corrected Recovery vol. % 98.1 97.7 - - - - - - - 98.0 97.7 - - - 97.9

Corrected Loss vol. % 0.9 1.3 - - - - - - - 1.0 1.3 - - - 1.1

DVPE (EPA equation) psi D5191 7.28 7.22 7.19 7.29 6.56 7.27 7.35 - - - 7.14 7.25 - 7.19 7.24

Aromatics vol. % D1319 - 15.1 - 14.7 15.3 - - 15.1 - - - - 14.4 15.4 15.0

Olefins vol. % D1319 - 9.6 - 8.9 8.4 - - 8.1 - - - - 8.8 9.0 8.8

Saturates vol. % * - - - - - - - - - - - - - - 65.6

Benzene vol. % D3606 - - - 0.66 - - 0.61 - - - - 0.64 0.69 0.82 0.68

S mg/kg D5453 23 28 23 24 - - 22 - - - - - - 22 23

RON - D2699 96.3 - 96.5 - - - 95.8 - - - - - - 96.4 96.3

MON - D2700 86.5 - 87.4 - - - 85.6 - - - - - - 86.9 86.6

(RON+MON)/2 - - 91.4 - 92.0 - - - 90.7 - - - - - - 91.7 91.5

C mass % D5291 mod.** 81.95 - - - 81.00 - - - - - - - 81.72 81.42 81.52

H mass % D5291 mod.** 14.14 - - - 14.13 - - - - - - - 14.30 14.26 14.21

O mass % D5599 - - 4.4 4.0 - - 3.8 - - - - 4.0 3.9 4.0 4.0

Net Heat of Combustion MJ/kg D4809 41.980 - - - - - 41.752 - - - - - - 41.624 41.785

Water mass % E-1064 - - - - - - 0.058 - - - - 0.087 - - 0.073

Lead g/l D3237 - - - - - - - - - - - - - - -

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 7 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7206 0.7209 - 0.7208 0.7208 - - - - - - - - - 0.7208

API Gravity, 60oF

o

API D4052 64.6 64.6 - 64.6 64.6 - - - - - - - - - 64.6

Ethanol vol. % D5599 - - - - - - <0.01 - - - - <0.10 <0.05 <0.10 <0.10

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 - - <0.10

Distillation IBP oF 96.2 100.7 102.7 100.2 - 97.5 100 - - 101.4 101.3 100.4 100.4 100 100.1

5% evap oF 126.9 129.0 130.5 122.1 - 124.3 125 - - 128.1 130.2 128.0 131.7 128 127.6

10% evap oF 136.1 138.1 138.6 133.4 - 134.9 136 - - 136.9 138.6 137.1 139.8 137 137.0

20% evap oF 148.7 149.3 149.9 146.2 - 147.8 148 - - 149.4 150.4 149.2 151.1 149 149.0

30% evap oF 161.5 161.8 162.5 159.2 - 160.2 161 - - 162.1 163.2 162.3 163.7 161 161.7

40% evap oF 176.5 176.8 176.7 174.4 - 175.6 176 - - 177.1 177.6 176.8 178.4 177 176.6

50% evap oF 192.9 193.5 193.5 191.7 - 192.3 192 - - 193.3 193.9 193.4 194.7 193 193.1

60% evap oF 209.8 210.9 210.4 208.9 - 209.9 209 - - 210.7 211.1 210 211.5 210 210.2

70% evap oF 227.8 229.7 228.7 227.3 - 228.6 228 - - 228.7 229.5 228.6 229.2 229 228.6

80% evap oF 248.8 252.5 251.8 249.6 - 250.8 251 - - 252.1 253.0 251.6 252.9 252 251.5

90% evap oF 296.9 298.8 299.7 293.5 - 299.8 298 - - 299.4 302.0 297.2 300.3 297 298.4

95% evap oF 327.3 329.9 331.3 326.8 - 328.7 329 - - 329.2 330.1 329.4 331.6 329 329.3

FBP oF 357.0 360.4 359.4 355.4 - 365.5 360 - - 358.3 382.5 359.6 362.8 359 361.8

Recovery vol. % 98.3 97.7 98.7 96.6 - 97.5 98.5 - - 98.4 98.4 97.7 98.6 97.9 98.1

Residue vol. % 1.0 1.1 0.8 0.6 - 1.1 1.0 - - 1.0 1.0 1.1 1.1 0.8 1.0

Loss vol. % 0.7 1.2 0.5 2.8 - 1.4 0.5 - - 0.6 0.6 1.2 0.3 1.3 1.0

Corrected Recovery vol. % 98.4 97.8 98.7 97.4 - - - - - 98.4 98.4 97.9 98.6 - 98.2

Corrected Loss vol. % 0.6 1.1 0.5 2.0 - - - - - 0.6 0.6 1.0 0.3 - 0.8

DVPE (EPA equation) psi D5191 7.19 7.22 7.06 7.17 6.45 7.00 7.22 - - - 7.13 7.07 - 7.32 7.15

Aromatics vol. % D1319 - 17.8 - 16.8 17.9 17.6 15.5 - - - - - 16.5 16.7 17.0

Olefins vol. % D1319 - 8.0 - 7.7 8.3 7.1 6.8 - - - - - 7.4 7.3 7.5

Saturates vol. % * - - - - - - - - - - - - - - 75.5

Benzene vol. % D3606 - - - 0.56 - - 0.51 - - - - 0.54 0.57 0.55 0.55

S mg/kg D5453 22 25 21 22 - - 24 - - - - - - 23 23

RON - D2699 91.2 - 91.3 - - - 91.2 - - - - - - 92.1 91.2

MON - D2700 84.4 - 83.9 - - - 84.2 - - - - - - 84.7 84.2

(RON+MON)/2 - - 87.8 - 87.6 - - - 87.7 - - - - - - 88.4 87.7

C mass % D5291 mod.** 85.20 - - - 84.40 - - - - - - - 85.72 85.32 85.16

H mass % D5291 mod.** 14.05 - - - 14.39 - - - - - - - 14.37 14.20 14.25

O mass % D5599 - - - - - - - - - - - <0.1 <0.01 - <0.1

Net Heat of Combustion MJ/kg D4809 43.872 - - - - - 43.548 - - - - - - 43.786 43.735

Water mass % E-1064 - - - - - - 0.005 - - - - 0.033 - - 0.019

Lead g/l D3237 - - - - - - <0.001 - - - - - - - <0.001

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 8 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7187 0.7192 - 0.7192 0.7191 - - - - - - - - - 0.7191

API Gravity, 60oF

o

API D4052 65.1 65.1 - 65.1 65.1 - - - - - - - - - 65.1

Ethanol vol. % D5599 - - - - - - <0.01 - - - - <0.10 <0.05 <0.10 <0.10

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 - - <0.10

Distillation IBP oF 79.7 79.8 91.2 85.7 - - 84 - - 82.4 79.9 83.8 86.7 84 83.7

5% evap oF 107.2 109.5 112.6 103.1 - - 100 - - 108.3 107.8 107.1 116.9 108 108.1

10% evap oF 122.4 124.7 126.9 118.8 - - 118 - - 123.4 123.2 122.2 130.3 124 123.4

20% evap oF 151.1 153.5 153.0 146.9 - - 148 - - 152.0 151.3 149.8 157.9 152 151.6

30% evap oF 180.9 182.9 180.9 177.9 - - 178 - - 181.7 180.5 220.8 185.6 182 185.1

40% evap oF 204.1 205.5 204.6 202.3 - - 203 - - 205.0 203.8 203.6 207.4 205 204.4

50% evap oF 220.6 221.7 220.6 220.3 - - 220 - - 221.3 220.5 220.8 222.7 222 221.1

60% evap oF 233.3 234.5 233.8 229.7 - - 234 - - 233.7 233.3 233.7 234.8 234 233.5

70% evap oF 245.5 246.9 246.0 245.1 - - 245 - - 247.2 246.1 245.2 248.5 248 246.4

80% evap oF 262.8 265.0 264.6 262.4 - - 263 - - 263.7 263.3 262.9 266.6 266 264.0

90% evap oF 301.3 304.2 304.3 299.2 - - 302 - - 304.3 302.1 299.5 310.0 304 303.1

95% evap oF 328.9 331.3 331.3 327.0 - - 330 - - 331.2 329.1 326.0 338.2 332 330.5

FBP oF 357.3 364.8 364.1 355.7 - - 363 - - 362.1 359.8 359.2 362.7 360 360.9

Recovery vol. % 97.5 97.9 97.6 96.65 - - 96.7 - - 97.6 97.2 97.7 97.7 96.9 97.5

Residue vol. % 1.0 1.0 0.9 0.1 - - 1.1 - - 1.0 1.0 0.9 1.1 1.1 0.9

Loss vol. % 1.5 1.1 1.5 3.3 - - 2.2 - - 1.4 1.8 1.4 1.2 2.0 1.7

Corrected Recovery vol. % 97.7 97.9 97.8 97.2 - - - - - 97.5 97.5 98.0 97.7 - 97.7

Corrected Loss vol. % 1.3 1.1 1.3 2.3 - - - - - 1.5 1.5 1.1 1.2 - 1.4

DVPE (EPA equation) psi D5191 10.16 10.43 10.00 10.25 9.41 - 10.32 - - - 10.24 10.25 - 9.93 10.20

Aromatics vol. % D1319 - 15.8 - 15.5 15.1 - 15.9 - - - - - 15.6 16.2 15.7

Olefins vol. % D1319 - 6.3 - 5.9 6.1 - 6.5 - - - - - 7.2 6.2 6.4

Saturates vol. % * - - - - - - - - - - - - - - 78.0

Benzene vol. % D3606 - - - 0.53 - - 0.48 - - - - 0.50 - 0.48 0.50

S mg/kg D5453 22 25 21 22 - - 26 - - - - - - 22 23

RON - D2699 95.2 - 95.6 - - - 95.5 - - - - - - 95.6 95.5

MON - D2700 87.7 - 87.7 - - - 87.6 - - - - - - 88.1 87.8

(RON+MON)/2 - - 91.5 - 91.7 - - - 91.6 - - - - - - 91.9 91.7

C mass % D5291 mod.** 84.69 - - - 84.75 - - - - - - - 85.56 85.49 85.12

H mass % D5291 mod.** 14.15 - - - 14.50 - - - - - - - 14.48 14.16 14.32

O mass % D5599 - - - - - - <0.1 - - - - <0.1 <0.01 - <0.1

Net Heat of Combustion MJ/kg D4809 44.046 - - - - - 44.098 - - - - - - 43.966 44.037

Water mass % E-1064 - - - - - - - - - - - 0.020 - - 0.020

Lead g/l D3237 - - - - - - 0.001 - - - - - - - 0.001

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 9 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7450 0.7453 - 0.7454 0.7459 - - - - - - - - - 0.7454

API Gravity, 60oF

o

API D4052 58.2 58.1 - 58.2 58.2 - - - - - - - - - 58.2

Ethanol vol. % D5599 - - - - - - <0.01 - - - - <0.10 <0.05 <0.10 <0.10

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 - - <0.10

Distillation IBP oF 82.2 84.4 91.2 88.3 85.1 - 85 - - 84.1 84.0 84.9 87.1 84 85.3

5% evap oF 105.4 106.9 108.1 103.0 104.9 - 103 - - 104.6 107.2 105.6 111.2 102 105.1

10% evap oF 114.9 116.6 117.3 112.9 115.3 - 115 - - 114.4 116.0 115.1 119.4 113 115.1

20% evap oF 130.3 132.1 131.2 128.0 131.0 - 131 - - 129.8 130.9 130.1 134.4 129 130.3

30% evap oF 147.3 149.0 147.2 144.9 147.7 - 149 - - 146.6 147.8 146.9 151.4 146 147.2

40% evap oF 168.0 170.1 167.9 164.9 167.5 - 169 - - 167.0 168.4 168.2 173.1 166 167.7

50% evap oF 193.2 195.3 192.6 190.2 192.6 - 194 - 192.1 194.2 192.5 199.2 191 192.8

60% evap oF 225.1 224.2 225.7 222.4 224.6 - 227 - - 224.7 226.7 223.9 231.9 223 224.7

70% evap oF 260.7 259.2 261.0 258.9 260.2 - 261 - - 260.4 261.7 259.6 265.7 260 260.3

80% evap oF 293.8 292.3 293.9 287.1 294.1 - 290 - - 292.6 294.8 291.7 299.0 292 292.2

90% evap oF 342.2 342.5 343.0 339.7 341.8 - 344 - - 341.7 341.2 340.9 349.5 341 341.8

95% evap oF 364.3 363.2 365.2 363.1 362.8 - 365 - - 362.5 363.0 363 367.8 363 363.5

FBP oF 381.1 384.4 385.0 375.9 387.7 - 387 - - 380.2 394.1 390.3 381.2 381 384.7

Recovery vol. % 98 98.0 97.8 96.6 98.1 - 97.8 - - 97.5 97.9 97.7 97.4 97.2 97.6

Residue vol. % 1.1 1.1 0.9 0.6 1.0 - 0.9 - - 1.1 1.1 0.8 1.0 0.5 1.0

Loss vol. % 0.9 0.9 1.3 2.8 1.0 - 1.3 - - 1.4 1.0 1.5 1.6 2.3 1.4

Corrected Recovery vol. % 98.1 97.9 98 97.6 - - - - - 97.4 98.0 98 97.4 - 97.9

Corrected Loss vol. % 0.8 1.0 1.1 1.8 - - - - - 1.5 0.9 1.2 1.6 - 1.2

DVPE (EPA equation) psi D5191 10.28 10.40 10.19 10.34 9.41 - 10.32 - - - 10.31 10.22 - 10.32 10.30

Aromatics vol. % D1319 - 36.1 - 35.7 35.1 - 35.7 - - - - - 34.6 37.3 35.8

Olefins vol. % D1319 - 7.5 - 6.1 6.4 - 5.5 - - - - - 6.2 6.2 6.2

Saturates vol. % * - - - - - - - - - - - - - - 58.0

Benzene vol. % D3606 - - - 0.57 - - 0.52 - - - - 0.52 - 0.55 0.54

S mg/kg D5453 23 27 22 23 - - 24 - - - - - - 23 23

RON - D2699 94.5 - 94.6 - - - 94.6 - - - - - - 94.3 94.5

MON - D2700 84.4 - 84.7 - - - 85.3 - - - - - - 84.9 84.8

(RON+MON)/2 - - 89.5 - 89.7 - - - 90.0 - - - - - - 89.6 89.7

C mass % D5291 mod.** 86.91 - - - 85.50 - - - - - - - 87.03 87.15 87.03

H mass % D5291 mod.** 12.65 - - - 12.84 - - - - - - - 13.02 12.78 12.82

O mass % D5599 - - - - - - <0.1 - - - - <0.1 <0.01 <0.1 <0.1

Net Heat of Combustion MJ/kg D4809 43.540 - - - - - 42.854 - - - - - - 43.234 43.209

Water mass % E-1064 - - - - - - 0.007 - - - - 0.011 - - 0.009

Lead g/l D3237 - - - - - - <0.001 - - - - - - - <0.001

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 10 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7641 0.7646 - 0.7644 0.7643 - - - - - - - - - 0.7644

API Gravity, 60oF

o

API D4052 53.4 53.4 - 53.4 53.4 - - - - - - - - - 53.4

Ethanol vol. % D5599 - - 10.35 9.88 - - 9.83 - - - - 9.82 9.70 9.87 9.82

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 0.06 - <0.10

Distillation IBP oF 103.8 103.7 - - - 107.4 - - 104.4 104.6 103.0 - - 106.1 104.7

5% evap oF 130.1 130.8 - - - 129.1 - - 130.5 129.2 129.9 - - 130.7 130.0

10% evap oF 136.7 136.7 - - - 135.9 - - 136.1 136.4 136.1 - - 136.5 136.3

20% evap oF 144.6 144.8 - - - 144.1 - - 144.1 144.1 144.2 - - 144.3 144.3

30% evap oF 151.1 152.0 - - - 151.1 - - 150.8 150.9 150.6 - - 150.7 151.0

40% evap oF 161.7 163.9 - - - 162.5 - - 160.1 161.8 158.4 - - 162.5 161.6

50% evap oF 215.7 217.4 - - - 217.2 - - 217.9 216.6 216.8 - - 218.4 217.1

60% evap oF 260.7 262.1 - - - 261.3 - - 261.9 260.8 261.2 - - 262.8 261.5

70% evap oF 285.9 292.1 - - - 291.1 - - 292.5 291.6 290.8 - - 288.6 290.4

80% evap oF 317.6 318.0 - - - 317.2 - - 317.7 316.9 316.3 - - 318.8 317.5

90% evap oF 340.2 340.3 - - - 339.2 - - 340.5 340.0 338.9 - - 342.2 340.2

95% evap oF 353.0 354.0 - - - 355.3 - - 353.8 354.0 353.4 - - 356.8 354.3

FBP oF 371.3 373.0 - - - 375.7 - - 371.3 369.9 374.7 - - 371.1 372.4

Recovery vol. % 98.4 98.5 - - - 97.9 - - 98.5 97.8 98.3 - - 98.0 98.3

Residue vol. % 1.0 1.0 - - - 1.0 - - 1.0 1.1 1.0 - - 1.0 1.0

Loss vol. % 0.6 0.5 - - - 1.1 - - 0.5 1.1 0.7 - - 1.0 0.7

Corrected Recovery vol. % 98.4 98.5 - - - - - - - 97.8 98.3 - - - 98.3

Corrected Loss vol. % 0.6 0.5 - - - - - - - 1.1 0.7 - - - 0.7

DVPE (EPA equation) psi D5191 7.19 7.19 7.08 7.16 6.45 7.00 7.19 - - - 7.10 7.08 - 7.02 7.11

Aromatics vol. % D1319 - 33.5 - 34.5 33.5 34.2 - - - - - - 32.7 35.6 34.0

Olefins vol. % D1319 - 7.5 - 6.2 6.1 6.6 - - - - - - 6.1 6.0 6.1

Saturates vol. % * - - - - - - - - - - - - - - 50.1

Benzene vol. % D3606 - - - 0.53 - - 0.50 - - - - 0.51 0.49 0.58 0.52

S mg/kg D5453 23 27 24 25 - - 25 - - - - - - 25 25

RON - D2699 98.5 - 98.6 - - - 99.7 - - - - - - 98.4 98.5

MON - D2700 86.8 - 87.4 - - - 86.7 - - - - - - 87.4 87.2

(RON+MON)/2 - - 92.7 - 93.0 - - - 93.2 - - - - - - 92.9 92.9

C mass % D5291 mod.** 83.46 - - - 82.85 - - - - - - - 83.45 83.49 83.47

H mass % D5291 mod.** 12.72 - - - 12.90 - - - - - - - 13.04 12.67 12.83

O mass % D5599 - - 3.7 3.6 - - 3.6 - - - - 3.5 3.5 3.6 3.6

Net Heat of Combustion MJ/kg D4809 41.486 - - - - - 40.770 - - - - - - 41.374 41.210

Water mass % E-1064 - - - - - - 0.058 - - - - 0.076 - - 0.067

Lead g/l D3237 - - - - - - <0.003 - - - - - - - <0.003

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 11 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7593 0.7598 - 0.7597 0.7597 - - - - - - - - - 0.7596

API Gravity, 60oF

o

API D4052 54.6 54.5 - 54.6 54.6 - - - - - - - - - 54.6

Ethanol vol. % D5599 - - 10.81 10.30 - - 9.92 - - - - 10.40 10.15 10.21 10.30

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 - - <0.10

Distillation IBP oF 90.4 92.0 - - - 94.2 - - 92.7 90.5 91.9 - - 92.1 92.0

5% evap oF 115.9 115.9 - - - 114.6 - - 113.7 115.6 116.4 - - 117.2 115.4

10% evap oF 124.5 124.9 - - - 123.9 - - 123.4 124.8 125.1 - - 125.4 124.4

20% evap oF 137.8 137.8 - - - 137.6 - - 137.1 137.7 137.6 - - 137.9 137.6

30% evap oF 148.3 148.3 - - - 148.2 - - 147.2 148.4 148.2 - - 148.3 148.1

40% evap oF 157.5 157.1 - - - 157.0 - - 155.1 156.6 155.6 - - 156.7 156.5

50% evap oF 189.6 188.4 - - - 190.0 - - 188.6 189.7 189.2 - - 196.4 189.3

60% evap oF 230.5 231.6 - - - 231.0 - - 230.0 231.8 231.5 - - 233.1 231.1

70% evap oF 251.3 252.4 - - - 251.0 - - 250.2 251.7 251.9 - - 252.9 251.4

80% evap oF 270.2 270.9 - - - 269.1 - - 269.4 269.8 270.7 - - 272.8 270.0

90% evap oF 297.7 299 - - - 299.0 - - 298.0 298.5 299.5 - - 302.8 298.6

95% evap oF 324.3 325.5 - - - 325.5 - - 323.4 324.9 326.1 - - 336.0 325.0

FBP oF 359.5 361.6 - - - 358.6 - - 358.0 358.9 368.0 - - 361.2 360.8

Recovery vol. % 98.4 97.6 - - - 97.5 - - 97.2 98.0 97.7 - - 97.9 97.9

Residue vol. % 1.0 1.0 - - - 1.0 - - 1.0 1.0 1.0 - - 1.0 1.0

Loss vol. % 0.6 1.4 - - - 1.5 - - 1.8 1.0 1.3 - - 1.1 1.1

Corrected Recovery vol. % 98.4 97.6 - - - - - - - 98.0 97.9 - - - 98.0

Corrected Loss vol. % 0.6 1.4 - - - - - - - 1.0 1.1 - - - 1.0

DVPE (EPA equation) psi D5191 9.91 10.03 9.76 9.99 9.11 - 10.02 - - - 9.95 9.91 - 9.87 9.93

Aromatics vol. % D1319 - 35.9 - 35.4 34.8 35.7 33.8 34.4 - - - - 17.4 35.1 35.0

Olefins vol. % D1319 - 7.5 - 6.6 7.1 7.0 7.2 6.8 - - - - 8.9 6.3 6.9

Saturates vol. % * - - - - - - - - - - - - - - 47.8

Benzene vol. % D3606 - - - 0.53 - - 0.50 - - - - 0.51 0.57 0.57 0.54

S mg/kg D5453 23 28 22 24 - - 27 - - - - - - 22 24

RON - D2699 97.8 - 98.2 - - - 97.4 - - - - - - 97.8 97.8

MON - D2700 85.6 - 86.3 - - - 85.0 - - - - - - 85.5 85.6

(RON+MON)/2 - - 91.7 - 92.3 - - - 91.2 - - - - - - 91.7 91.7

C mass % D5291 mod.** 83.65 - - - 83.10 - - - - - - - 83.67 83.71 83.68

H mass % D5291 mod.** 12.44 - - - 12.74 - - - - - - - 12.76 12.50 12.61

O mass % D5599 - - 3.9 3.7 - - 3.6 - - - - 3.8 3.7 3.7 3.7

Net Heat of Combustion MJ/kg D4809 41.462 - - - - - 40.970 - - - - - - 41.092 41.175

Water mass % E-1064 - - - - - - 0.055 - - - - 0.076 - - 0.0655

Lead g/l D3237 - - - - - - - - - - - - - - -

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - 0.5 - - - - - - - 0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 12 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7514 0.7518 - 0.7518 0.7517 - - - - - - - - - 0.7517

API Gravity, 60oF

o

API D4052 56.6 56.5 - 56.5 56.5 - - - - - - - - - 56.5

Ethanol vol. % D5599 - - 10.63 9.91 - - 9.83 - - - - 9.89 9.68 9.85 9.83

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 - - <0.10

Distillation IBP oF 90.6 89.9 - - - 92.1 - - 92.9 89.4 92.7 - - 91.6 91.3

5% evap oF 110.1 110.5 - - - 110.8 - - 111.9 109.3 111.3 - - 111.4 110.7

10% evap oF 116.4 116.6 - - - 117.0 - - 117.6 116.3 117.5 - - 116.9 116.9

20% evap oF 124.8 125.5 - - - 123.8 - - 125.5 125.1 125.5 - - 124.2 125.0

30% evap oF 133.6 134.1 - - - 133.2 - - 133.9 133.7 134.1 - - 134.0 133.8

40% evap oF 142.4 142.8 - - - 142.3 - - 143.0 143.1 143.3 - - 143.0 142.8

50% evap oF 152.6 152.8 - - - 151.3 - - 151.5 152.1 153.0 - - 153.3 152.2

60% evap oF 196.0 197.6 - - - 200.1 - - 200.8 198.0 198.3 - - 210.2 198.5

70% evap oF 273.9 275.0 - - - 275.5 - - 276.0 274.7 275.3 - - 280.4 275.1

80% evap oF 307.6 308.1 - - - 307.7 - - 308.0 307.7 308.0 - - 312.2 307.9

90% evap oF 339.9 340.3 - - - 340.1 - - 339.4 339.4 339.9 - - 341.7 339.8

95% evap oF 357.8 357.8 - - - 357.5 - - 357.0 358.0 358.3 - - 365.0 357.7

FBP oF 376.3 377.8 - - - 376.3 - - 373.6 373.4 378.0 - - 379.5 375.9

Recovery vol. % 98.0 97.8 - - - 97.8 - - 97.4 97.8 97.8 - - 97.5 97.9

Residue vol. % 1.1 1.1 - - - 1.1 - - 1.1 1.1 1.1 - - 1.1 1.1

Loss vol. % 0.9 1.1 - - - 1.1 - - 1.5 1.1 1.1 - - 1.4 1.1

Corrected Recovery vol. % 98.1 97.8 - - - - - - - 97.8 98.0 - - - 97.9

Corrected Loss vol. % 0.8 1.1 - - - - - - - 1.1 0.9 - - - 1.0

DVPE (EPA equation) psi D5191 10.15 10.18 9.99 10.23 9.35 - 10.20 - - - 10.13 10.01 - 10.14 10.13

Aromatics vol. % D1319 - 34.3 - 35.4 34.5 - - 34.6 - - - - 38.0 35.1 34.8

Olefins vol. % D1319 - 8.0 - 6.8 6.8 - - 6.4 - - - - 7.5 6.0 6.9

Saturates vol. % * - - - - - - - - - - - - - - 48.5

Benzene vol. % D3606 - - - 0.57 - - 0.52 - - - - 0.55 0.60 0.62 0.57

S mg/kg D5453 19 22 17 18 - - 21 - - - - - - 19 19

RON - D2699 101.2 - 100.4 - - - 99.9 - - - - - - 100.0 100.4

MON - D2700 87.4 - 87.9 - - - 88.5 - - - - - - 88.1 88.0

(RON+MON)/2 - - 94.3 - 94.2 - - - 94.2 - - - - - - 94.1 94.2

C mass % D5291 mod.** 84.31 - - - 81.80 - - - - - - - 83.40 83.76 83.32

H mass % D5291 mod.** 12.26 - - - 12.72 - - - - - - - 13.00 12.74 12.68

O mass % D5599 - - 3.9 3.6 - - 3.6 - - - - 3.6 3.6 3.6 3.6

Net Heat of Combustion MJ/kg D4809 41.648 - - - - - 41.084 - - - - - - 41.388 41.373

Water mass % E-1064 - - - - - - 0.053 - - - - 0.078 - - 0.066

Lead g/l D3237 - - - - - - <0.003 - - - - - - - <0.003

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 13 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7537 0.7541 - 0.7541 0.7540 - - - - - - - - - 0.7540

API Gravity, 60oF

o

API D4052 56.0 56.0 - 56.0 56.0 - - - - - - - - - 56.0

Ethanol vol. % D5599 - - - - - - <0.01 - - - - <0.10 <0.05 <0.10 <0.10

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 - - <0.10

Distillation IBP oF 93.5 94.9 100.6 96.0 97.7 93.2 99 - 93.8 93.8 97.2 97.7 102.0 97 96.6

5% evap oF 126.1 129.3 131.0 123.2 125.2 125.6 123 - 123.8 126.6 129.9 129.4 135.2 123 127.0

10% evap oF 139.3 141.7 142.5 135.7 138.6 137.9 137 - 137.6 139.6 141.7 142.2 146.3 137 139.8

20% evap oF 158.7 160.7 160.0 154.9 157.6 156.8 157 - 157.2 158.5 159.4 160.9 163.8 157 158.7

30% evap oF 178.7 179.6 179.4 175.0 177.1 176.8 177 - 176.6 178.1 179.4 180.3 181.1 177 178.2

40% evap oF 200.4 200.6 201.0 198.1 198.9 198.9 199 - 198.4 199.9 200.7 201.7 203.2 198 199.9

50% evap oF 222.8 223.4 223.0 220.8 221.7 221.0 222 - 221.1 223.0 223.3 223.6 225.0 222 222.5

60% evap oF 245.2 245.3 245.8 242.8 244.9 244.5 245 - 244.0 245.7 246.0 246.3 246.7 245 245.2

70% evap oF 269.9 269.5 270.5 268.2 269.4 269.2 270 - 268.4 269.8 270.2 270.8 271.2 270 269.8

80% evap oF 303.7 304.0 305.1 301.2 302.5 302.5 305 - 301.7 302.4 304.3 303.9 306.0 303 303.5

90% evap oF 338.2 338.5 339.3 336.8 336.6 337.2 337 - 336.7 337.7 338.2 338.4 339.6 339 337.9

95% evap oF 354.4 354.4 355.8 352.1 353.3 353.7 356 - 353.1 354.0 353.5 354.8 356.5 355 354.4

FBP oF 376.6 379.0 374.9 370.3 379.0 375.6 385 - 373.6 375.8 384.0 376.9 379.3 377 377.5

Recovery vol. % 97.9 98.0 98.7 98.0 97.1 97.7 98.5 - 97.5 98.1 98.1 98.3 98.4 96.9 98.2

Residue vol. % 1.1 1.1 0.8 0.4 1.2 1.1 0.9 - 1.1 1.1 1.1 1.0 1.0 1.0 1.0

Loss vol. % 1.0 0.9 0.5 1.6 1.7 1.2 0.6 - 1.4 0.8 0.8 0.7 0.6 2.1 0.9

Corrected Recovery vol. % 98.0 98.0 98.7 98.3 - - - - - 98.1 98.2 98.4 98.4 - 98.3

Corrected Loss vol. % 0.9 0.9 0.5 1.3 - - - - - 0.8 0.7 0.6 0.6 - 0.8

DVPE (EPA equation) psi D5191 6.92 6.98 6.86 6.98 6.28 6.77 6.96 - - - 6.96 6.89 - 6.92 6.9

Aromatics vol. % D1319 - 34.9 - 34.2 33.4 34.7 33.9 - - - - - 34.1 33.5 34.1

Olefins vol. % D1319 - 7.4 - 6.5 6.8 6.5 5.2 - - - - - 6.6 5.1 6.3

Saturates vol. % * - - - - - - - - - - - - - - 59.6

Benzene vol. % D3606 - - - 0.53 - - 0.49 - - - - 0.50 - 0.53 0.51

S mg/kg D5453 21 25 21 22 - - 26 - - - - - - 22 23

RON - D2699 95.7 - 95.9 - - - 95.8 - - - - - - 95.9 95.8

MON - D2700 85.8 - 85.7 - - - 86.1 - - - - - - 85.6 85.8

(RON+MON)/2 - - 90.8 - 90.8 - - - 91.0 - - - - - - 90.8 90.8

C mass % D5291 mod.** 87.07 - - - 86.44 - - - - - - - 86.9 86.63 86.76

H mass % D5291 mod.** 12.74 - - - 13.11 - - - - - - - 13.16 13.60 13.15

O mass % D5599 - - - - - - <0.1 - - - - <0.1 <0.01 <0.1 <0.1

Net Heat of Combustion MJ/kg D4809 43.230 - - - - - 43.184 - - - - - - 43.098 43.171

Water mass % E-1064 - - - - - - - - - - - 0.014 - - 0.014

Lead g/l D3237 - - - - - - <0.001 - - - - - - - <0.001

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - 1.5 - - - - - - - 1.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 14 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7220 0.7228 - 0.7223 0.7222 - - - - - - - - - 0.7223

API Gravity, 60oF

o

API D4052 64.2 64.1 - 64.2 64.2 - - - - - - - - - 64.2

Ethanol vol. % D5599 - - - - - - <0.10 - - - - <0.10 <0.05 <0.10 <0.10

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 - - <0.10

Distillation IBP oF 98.9 99.6 101.3 99.1 102.9 - 101 - - 99.2 103.1 99.0 100.7 99 100.4

5% evap oF 126.4 127.9 129.4 122.9 127.2 - 123 - - 126.4 128.3 125.7 130.4 124 126.5

10% evap oF 135.5 137.0 136.9 132.6 136.0 - 134 - - 135.4 136.0 134.9 137.8 134 135.5

20% evap oF 147.5 148.8 148.1 144.7 147.0 - 146 - - 147.6 147.7 146.8 149.4 146 147.3

30% evap oF 160.2 161.4 160.5 157.9 159.6 - 159 - - 160.4 160.4 159.5 161.8 159 160.0

40% evap oF 175.7 176.4 175.5 173.2 174.6 - 174 - - 175.7 175.7 174.4 177.4 174 175.1

50% evap oF 192.7 193.7 192.9 191.1 192.2 - 193 - - 193.5 193.3 192.3 195.0 192 192.8

60% evap oF 211.7 212.8 212.9 210.7 211.5 - 212 - - 212.6 212.9 211.5 213.8 210 212.0

70% evap oF 237.1 238.4 238.6 234.5 235.8 - 237 - - 238.1 237.9 236.6 239.5 236 237.3

80% evap oF 280.6 281.7 280.8 275.7 279.9 - 281 - - 279.8 281.5 278.3 284.7 277 280.1

90% evap oF 337.8 339.0 340.0 337.5 338.5 - 338 - - 337.6 339.5 337.7 340.4 338 338.5

95% evap oF 354.8 354.0 355.6 353.4 354.6 - 355 - - 354.4 354.2 353.8 355.7 354 354.5

FBP oF 372.4 373.6 373.5 366.7 380.3 - 388 - - 373.2 381.5 385.9 374.2 369 377.5

Recovery vol. % 98.1 97.9 98.6 97.0 98.8 - 98.5 - - 98.0 97.6 98.0 98.7 97.7 98.0

Residue vol. % 1.1 1.1 0.9 0.8 1.0 - 0.9 - - 1.1 1.1 0.7 1.0 0.6 1.0

Loss vol. % 0.8 1.0 0.5 2.2 0.2 - 0.6 - - 0.9 1.3 1.3 0.3 1.7 1.0

Corrected Recovery vol. % 98.2 97.6 98.6 97.6 - - - - - 98.0 97.9 98.2 98.7 - 98.1

Corrected Loss vol. % 0.7 1.0 0.5 1.6 - - - - - 0.9 1.0 1.1 0.3 - 0.9

DVPE (EPA equation) psi D5191 7.25 7.23 6.99 7.24 6.77 - 7.31 - - - 7.17 7.22 - 7.09 7.14

Aromatics vol. % D1319 - 16.9 - 16.2 17.0 - 17.0 - - - - - 17.9 16.6 16.9

Olefins vol. % D1319 - 9.3 - 8.8 9.0 - 7.6 - - - - - 8.5 7.7 8.5

Saturates vol. % * - - - - - - - - - - - - - - 74.6

Benzene vol. % D3606 - - - 0.54 - - 0.49 - - - - 0.51 0.53 0.52 0.52

S mg/kg D5453 23 27 23 23 - - 25 - - - - - - 24 24

RON - D2699 91.1 - 91.7 - - - 91.5 - - - - - - 91.5 91.5

MON - D2700 84.3 - 84.5 - - - 85.1 - - - - - - 84.6 84.6

(RON+MON)/2 - - 87.7 - 88.1 - - - 88.3 - - - - - - 88.1 88.1

C mass % D5291 mod.** 84.82 - - - 85.21 - - - - - - - 85.66 85.42 85.28

H mass % D5291 mod.** 13.96 - - - 14.55 - - - - - - - 14.39 14.24 14.29

O mass % D5599 - - - - - - - - - - - <0.1 <0.01 - <0.1

Net Heat of Combustion MJ/kg D4809 44.000 - - - - - 42.770 - - - - - - 43.786 43.519

Water mass % E-1064 - - - - - - 0.005 - - - - 0.024 - - 0.015

Lead g/l D3237 - - - - - - <0.001 - - - - - - - <0.001

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 15 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7424 0.7428 - 0.7428 0.7430 - - - - - - - - - 0.7428

API Gravity, 60oF

o

API D4052 58.8 58.8 - 58.8 58.8 - - - - - - - - - 58.8

Ethanol vol. % D5599 - - - - - - <0.01 - - - - <0.10 <0.05 <0.10 <0.10

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 - - <0.10

Distillation IBP oF 80.8 83.3 92.3 88.3 - 81.1 84 - - 85.5 86.3 85.2 86.8 80 84.7

5% evap oF 105.9 106.2 108.5 103.9 - 104.3 102 - - 105.9 107.2 105.2 111.2 106 105.5

10% evap oF 115.4 116.4 118.2 113.6 - 114.4 114 - - 116.0 116.5 115.3 119.5 116 115.6

20% evap oF 130.9 131.3 131.9 128.4 - 129.8 130 - - 131.2 130.6 130.2 134.0 131 130.5

30% evap oF 147.2 147.8 147.4 144.6 - 145.9 146 - - 147.6 146.6 146.2 150.8 147 146.6

40% evap oF 167.0 167.6 166.6 164.2 - 165.5 167 - - 167.1 166.0 166.0 170.6 166 166.3

50% evap oF 190.4 190.6 189.7 188.0 - 189.3 190 - - 190.5 189.4 189.0 194.0 190 189.7

60% evap oF 216.6 217.1 216.5 214.4 - 215.4 217 - - 217.6 216.2 215.3 220.2 216 216.2

70% evap oF 243.2 244 243.9 241.9 - 241.8 242 - - 243.5 242.9 242.4 245.9 244 243.0

80% evap oF 266.0 266.7 266.9 265.0 - 264.7 265 - - 265.9 266.1 265.8 268.9 267 265.9

90% evap oF 299.2 300.5 299.5 298.3 - 298.3 300 - - 299.9 299.0 300.0 305.2 299 299.4

95% evap oF 328.2 331.2 331.3 327.2 - 327.3 330 - - 331.4 329.8 328.4 337.6 328 329.3

FBP oF 363.0 368.6 363.2 360.4 - 362.4 366 - - 361.0 364.0 363.2 366.5 365 363.7

Recovery vol. % 98.4 97.6 97.8 96.8 - 98.1 98.0 - - 97.4 97.3 97.1 97.9 97.8 97.5

Residue vol. % 1.0 1.0 0.8 0.5 - 1.0 0.9 - - 1.0 1.0 1.1 1.1 0.8 0.9

Loss vol. % 0.6 1.4 1.4 2.7 - 0.9 1.0 - - 1.6 1.7 1.8 1.0 1.4 1.6

Corrected Recovery vol. % 98.4 97.6 98.0 97.7 - - - - - 97.2 97.8 97.4 97.9 - 97.7

Corrected Loss vol. % 0.6 1.4 1.2 1.8 - - - - - 1.8 1.2 1.5 1.0 - 1.4

DVPE (EPA equation) psi D5191 10.33 10.37 9.92 10.36 9.45 10.12 10.26 - - - 10.31 10.30 - 10.06 10.23

Aromatics vol. % D1319 - 36.1 - 35.6 34.6 35.4 33.4 - - - - - 35.4 36.7 35.3

Olefins vol. % D1319 - 7.6 - 7.2 7.2 7.0 6.3 - - - - - 8.2 7.2 7.2

Saturates vol. % * - - - - - - - - - - - - - - 57.4

Benzene vol. % D3606 - - - 0.54 - - 0.49 - - - - 0.51 0.61 0.53 0.54

S mg/kg D5453 22 27 22 23 - - 25 - - - - - - 23 24

RON - D2699 95.1 - 95.1 - - - 94.9 - - - - - - 94.7 95.0

MON - D2700 84.6 - 84.7 - - - 85.2 - - - - - - 84.9 84.9

(RON+MON)/2 - - 89.9 - 89.9 - - - 90.1 - - - - - - 89.8 90.0

C mass % D5291 mod.** 87.36 - - - 85.93 - - - - - - - 87.17 87.06 86.88

H mass % D5291 mod.** 12.34 - - - 13.00 - - - - - - - 12.89 12.91 12.79

O mass % D5599 - - - - - - <0.1 - - - - <0.1 <0.01 - <0.1

Net Heat of Combustion MJ/kg D4809 43.442 - - - - - 42.750 - - - - - - 43.132 43.108

Water mass % E-1064 - - - - - - 0.007 - - - - 0.016 - - 0.012

Lead g/l D3237 - - - - - - <0.001 - - - - - - - <0.001

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - 0.5 - - - - - - - 0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 16 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7633 0.7638 - 0.7636 0.7635 - - - - - - - - - 0.7636

API Gravity, 60oF

o

API D4052 53.6 53.6 - 53.6 53.6 - - - - - - - - - 53.6

Ethanol vol. % D5599 - - 11.20 10.65 - - 10.69 - - - - 10.57 10.84 10.62 10.76

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.10 - - <0.10

Distillation IBP oF 102.4 103.8 - - - 107.2 - - 104.7 101.9 106.1 - - 105.6 104.5

5% evap oF 131.7 132.0 - - - 134.0 - - 134.8 131.3 133.6 - - 133.9 133.0

10% evap oF 138.7 138.4 - - - 139.5 - - 140.0 138.5 139.5 - - 139.5 139.2

20% evap oF 147.5 147.6 - - - 147.6 - - 148.5 147.5 148.1 - - 148.1 147.8

30% evap oF 155.3 155.3 - - - 154.8 - - 153.5 155.0 155.8 - - 156.0 155.1

40% evap oF 168.5 165.7 - - - 177.2 - - 180.0 169.6 169.1 - - 174.7 172.1

50% evap oF 217.4 215.9 - - - 220.6 - - 220.6 218.5 217.7 - - 220.9 218.8

60% evap oF 237.5 236.3 - - - 238.0 - - 238.6 237.6 236.5 - - 238.1 237.5

70% evap oF 250.8 250.2 - - - 252.1 - - 253.0 251.4 252.0 - - 253.5 251.9

80% evap oF 267.8 268.0 - - - 268.1 - - 269.8 267.8 267.7 - - 271.0 268.6

90% evap oF 299.6 297.8 - - - 300.0 - - 302.0 298.8 299.8 - - 306.1 300.6

95% evap oF 329.0 326.7 - - - 329.0 - - 333.3 326.2 329.3 - - 342.2 330.8

FBP oF 362.7 366.4 - - - 367.8 - - 364.5 358.8 369.1 - - 369.8 365.6

Recovery vol. % 98.4 97.8 - - - 98.5 - - 98.3 97.7 98.5 - - 97.6 98.1

Residue vol. % 1.0 1.0 - - - 1.0 - - 1.0 1.0 1.0 - - 1.0 1.0

Loss vol. % 0.6 1.2 - - - 0.5 - - 0.7 1.3 0.5 - - 1.4 0.9

Corrected Recovery vol. % 98.4 97.8 - - - - - - - 97.6 98.5 - - - 98.1

Corrected Loss vol. % 0.6 1.2 - - - - - - - 1.4 0.5 - - - 0.9

DVPE (EPA equation) psi D5191 7.18 7.22 7.02 7.19 6.46 - 7.08 - - - 7.14 7.16 - 7.00 7.12

Aromatics vol. % D1319 - 35.2 - 35.2 34.5 36.2 34.6 35.6 - - - - 37.1 36.7 35.6

Olefins vol. % D1319 - 7.9 - 6.7 6.1 5.5 6.6 5.9 - - - - 8.6 6.7 6.8

Saturates vol. % * - - - - - - - - - - - - - - 46.9

Benzene vol. % D3606 - - - 0.63 - - 0.60 - - - - 0.61 0.60 0.65 0.62

S mg/kg D5453 21 25 20 23 - - 26 - - - - - - 22 23

RON - D2699 101.5 - 101.0 - - - 100.8 - - - - - - 100.8 101.0

MON - D2700 87.9 - 88.6 - - - 88.1 - - - - - - 88.4 88.3

(RON+MON)/2 - - 94.7 - 94.8 - - - 94.5 - - - - - - 94.6 94.7

C mass % D5291 mod.** 83.45 - - - 81.99 - - - - - - - 83.42 83.32 83.40

H mass % D5291 mod.** 12.44 - - - 12.68 - - - - - - - 12.87 12.64 12.66

O mass % D5599 - - 4.0 3.9 - - 3.9 - - - - 3.8 3.9 3.8 3.9

Net Heat of Combustion MJ/kg D4809 41.210 - - - - - 40.860 - - - - - - 40.970 41.013

Water mass % E-1064 - - - - - - 0.057 - - - - 0.074 - - 0.066

Lead g/l D3237 - - - - - - - - - - - - - - -

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - 1.0 - - - - - - - 1.0

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 20 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7423 0.7427 - 0.7425 0.7424 - - - - - - - - - 0.7425

API Gravity, 60oF

o

API D4052 58.9 58.8 - 58.9 58.9 - - - - - - - - - 58.9

Ethanol vol. % D5599 - - 22.03 20.90 - - 20.33 - - - - 18.50 - 19.77 20.31

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - 0.03 - - - - <0.1 - - <0.10

Distillation IBP oF 109.7 108.1 - - - 107.6 - - 106.3 107.8 108.6 - - 107.4 107.9

5% evap oF 137.6 138.7 - - - 135.6 - - 137.7 137.0 137.4 - - 137.4 137.3

10% evap oF 142.9 143.2 - - - 141.7 - - 142.7 142.6 142.8 - - 142.5 142.6

20% evap oF 150.0 150.2 - - - 149.1 - - 149.7 149.8 149.8 - - 149.4 149.7

30% evap oF 155.6 155.5 - - - 155.0 - - 155.3 155.4 155.2 - - 154.9 155.3

40% evap oF 159.9 159.8 - - - 159.3 - - 159.4 160.0 159.9 - - 159.1 159.6

50% evap oF 162.9 162.6 - - - 162.2 - - 162.7 163.7 163.0 - - 162.0 162.7

60% evap oF 178.3 181 - - - 176.8 - - 186.3 177.7 176.5 - - 182.4 179.9

70% evap oF 233.2 234.7 - - - 235.9 - - 234.0 236.1 236.1 - - 233.6 234.8

80% evap oF 254.6 253.3 - - - 253.7 - - 252.0 253.9 253.4 - - 251.1 253.1

90% evap oF 299.1 298.8 - - - 297.3 - - 300.9 296.1 298.5 - - 300.2 298.7

95% evap oF 337.2 337.2 - - - 335.2 - - 339.4 334.2 335.2 - - 338.0 336.6

FBP oF 375.0 373.5 - - - 373.3 - - 368.1 362.6 374.2 - - 376.6 371.9

Recovery vol. % 98.5 98.9 - - - 98.4 - - 98.5 97.9 98.4 - - 98.8 98.4

Residue vol. % 1.0 1.0 - - - 1.0 - - 1.0 1.1 1.0 - - 1.0 1.0

Loss vol. % 0.5 0.1 - - - 0.6 - - 0.5 1.0 0.6 - - 0.2 0.6

Corrected Recovery vol. % 98.5 98.9 - - - - - - - 97.9 98.4 - - - 98.4

Corrected Loss vol. % 0.5 0.1 - - - - - - - 1.0 0.6 - - - 0.6

DVPE (EPA equation) psi D5191 6.72 6.73 6.59 6.73 6.08 6.70 6.79 - - - 6.71 6.64 - 6.70 6.70

Aromatics vol. % D1319 - 14.9 - 14.7 15.7 14.3 - 15.4 - - - - - 16.3 15.2

Olefins vol. % D1319 - 8.4 - 7.7 7.3 7.2 - 6.0 - - - - - 7.3 7.4

Saturates vol. % * - - - - - - - - - - - - - - 57.1

Benzene vol. % D3606 - - - 0.60 - - 0.57 - - - - 0.59 - 0.69 0.61

S mg/kg D5453 20 23 20 21 - - 22 - - - - - - 23 22

RON - D2699 102.3 - 101.8 - - - 101.6 - - - - - - 101.8 101.9

MON - D2700 88.8 - 89.5 - - - 89.0 - - - - - - 89.8 89.3

(RON+MON)/2 - - 95.6 - 95.7 - - - 95.3 - - - - - - 95.8 95.6

C mass % D5291 mod.** 78.13 - - - 77.55 - - - - - - - 78.57 78.00 78.06

H mass % D5291 mod.** 13.85 - - - 13.86 - - - - - - - 14.06 14.26 14.01

O mass % D5599 - - 8.2 7.8 - - 7.6 - - - - 6.9 - 7.4 7.58

Net Heat of Combustion MJ/kg D4809 40.072 - - - - - 40.104 - - - - - - 39.996 40.057

Water mass % E-1064 - - - - - - - - - - - 0.138 - - 0.138

Lead g/l D3237 - - - - - - <0.0003 - - - - - - - <0.003

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 21 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7751 0.7756 - 0.7755 0.7753 - - - - - - - - - 0.7754

API Gravity, 60oF

o

API D4052 50.8 50.8 - 50.8 50.8 - - - - - - - - - 50.8

Ethanol vol. % D5599 - - 20.95 20.90 - - 20.32 - - - - 18.51 - 20.04 20.14

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.1 - - <0.10

Distillation IBP oF 103.4 103.7 - - - 111.8 - - 108.6 103.6 103.8 - - 109.3 106.3

5% evap oF 133.3 133.7 - - - 135.6 - - 137.1 132.7 134.8 - - 135.9 134.7

10% evap oF 140.6 140.8 - - - 141.8 - - 142.6 140.4 141.4 - - 141.7 141.3

20% evap oF 150.1 149.9 - - - 150.9 - - 150.9 149.5 150.1 - - 150.4 150.3

30% evap oF 157.0 156.7 - - - 157.5 - - 157.6 156.7 157.0 - - 157.4 157.1

40% evap oF 162.5 162.4 - - - 162.7 - - 162.7 162.7 162.3 - - 162.7 162.6

50% evap oF 167.2 167.3 - - - 168.1 - - 167.7 167.9 167.0 - - 168.1 167.6

60% evap oF 214.4 213.1 - - - 217.5 - - 224.5 211.8 216.4 - - 223.1 217.3

70% evap oF 255.4 255.3 - - - 253.4 - - 256.5 255.7 254.9 - - 255.2 255.2

80% evap oF 276.0 275.3 - - - 273.5 - - 274.6 274.4 275.8 - - 277.2 275.3

90% evap oF 305.5 304.6 - - - 303.7 - - 305.6 302.3 305.3 - - 307.8 305.0

95% evap oF 330.2 330.2 - - - 329.2 - - 334.5 329.1 331.3 - - 334.3 331.3

FBP oF 360.6 363.9 - - - 359.4 - - 361.9 354.5 363.2 - - 359.8 360.5

Recovery vol. % 98.4 97.9 - - - 98.4 - - 98.4 98.0 98.5 - - 98.2 98.2

Residue vol. % 1.0 1.0 - - - 1.0 - - 1.0 1.0 1.0 - - 1.0 1.0

Loss vol. % 0.6 1.1 - - - 0.6 - - 0.6 1.0 0.5 - - 0.8 0.8

Corrected Recovery vol. % 98.4 97.9 - - - - - - - 98.0 98.5 - - - 98.2

Corrected Loss vol. % 0.6 1.1 - - - - - - - 1.0 0.5 - - - 0.8

DVPE (EPA equation) psi D5191 7.14 7.17 7.03 7.12 6.40 - 6.98 - - - 7.11 6.95 - 6.94 7.06

Aromatics vol. % D1319 - 36.7 - 35.0 34.9 37.0 - 35.0 - - - - 35.2 34.5 35.5

Olefins vol. % D1319 - 8.0 - 7.6 7.0 7.3 - 6.6 - - - - 6.3 7.1 7.1

Saturates vol. % * - - - - - - - - - - - - - - 37.3

Benzene vol. % D3606 - - - 0.56 - - 0.52 - - - - 0.53 0.73 0.72 0.61

S mg/kg D5453 20 25 19 22 - - 27 - - - - - - 20 22

RON - D2699 102.2 - 101.3 - - - 101.6 - - - - - - 100.3 101.4

MON - D2700 86.8 - 88.2 - - - 86.8 - - - - - - 88.1 87.5

(RON+MON)/2 - - 94.5 - 94.8 - - - 94.2 - - - - - - 94.2 94.5

C mass % D5291 mod.** 79.55 - - - 79.15 - - - - - - - 80.20 80.70 79.90

H mass % D5291 mod.** 12.23 - - - 12.70 - - - - - - - 12.54 12.24 12.43

O mass % D5599 - - 7.4 7.4 - - 7.2 - - - - 6.6 - 7.1 7.1

Net Heat of Combustion MJ/kg D4809 39.392 - - - - - 39.182 - - - - - - 39.280 39.285

Water mass % E-1064 - - - - - - - - - - - 0.128 - - 0.128

Lead g/l D3237 - - - - - - 0.009 - - - - - - - 0.009

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - 0.5 - - - - - - - 0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 22 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7368 0.7372 - 0.7372 0.7372 - - - - - - - - - 0.7371

API Gravity, 60oF

o

API D4052 60.3 60.2 - 60.3 60.3 - - - - - - - - - 60.3

Ethanol vol. % D5599 - - 22.12 21.22 - - 20.58 - - - - 18.57 - 20.06 20.51

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.1 - - <0.10

Distillation IBP oF 84.7 90.0 - - - 92.5 - - 91.7 91.3 88.6 - - 93.0 89.8

5% evap oF 119.4 118.0 - - - 119.7 - - 119.8 118.1 117.9 - - 120.5 118.8

10% evap oF 129.9 128.8 - - - 130.4 - - 130.1 129.0 129.1 - - 130.1 129.6

20% evap oF 144.8 143.6 - - - 144.5 - - 144.4 144.2 144.2 - - 144.7 144.3

30% evap oF 154.1 153.7 - - - 153.6 - - 153.5 153.6 153.8 - - 153.8 153.7

40% evap oF 160.0 159.6 - - - 159.2 - - 159.1 159.7 159.6 - - 159.1 159.5

50% evap oF 163.6 163.7 - - - 162.9 - - 162.0 163.6 163.1 - - 162.6 163.2

60% evap oF 168.2 166.3 - - - 168.2 - - 165.5 168.3 166.7 - - 168.2 167.2

70% evap oF 234.5 233.4 - - - 234.0 - - 233.7 233.7 233.9 - - 234.4 233.9

80% evap oF 250.4 253.0 - - - 254.9 - - 254.4 254.8 254.0 - - 256.5 253.6

90% evap oF 297.4 298.1 - - - 296.4 - - 298.3 296.3 297.5 - - 303.4 297.3

95% evap oF 333.9 336.2 - - - 333.3 - - 334.6 333.9 334.8 - - 342.8 334.5

FBP oF 372.9 374.7 - - - 364.2 - - 371.4 362.0 374.0 - - 377.2 369.9

Recovery vol. % 98.9 97.4 - - - 98.1 - - 97.2 97.3 97.6 - - 97.8 97.8

Residue vol. % 1.0 1.1 - - - 1.0 - - 1.1 1.1 1.1 - - 1.0 1.1

Loss vol. % 0.1 1.5 - - - 0.9 - - 1.7 1.6 1.3 - - 1.2 1.1

Corrected Recovery vol. % 98.8 97.5 - - - - - - - 97.3 97.8 - - - 97.9

Corrected Loss vol. % 0.2 1.4 - - - - - - - 1.6 1.1 - - - 1.1

DVPE (EPA equation) psi D5191 10.05 10.31 9.93 10.27 9.38 10.31 - - - - 10.17 10.11 - 10.22 10.21

Aromatics vol. % D1319 - 14.9 - 14.5 15.0 15.3 - 14.6 - - - - - 15.4 15.0

Olefins vol. % D1319 - 7.9 - 6.2 7.3 6.3 - 6.6 - - - - - 7.1 6.9

Saturates vol. % * - - - - - - - - - - - - - - 57.6

Benzene vol. % D3606 - - - 0.59 - 0.56 - - - - - 0.57 - 0.65 0.59

S mg/kg D5453 20 23 20 20 - - 21 - - - - - - 21 21

RON - D2699 102.2 - 101.7 - - - 101.8 - - - - - - 101.3 101.8

MON - D2700 88.6 - 89.3 - - - 89.8 - - - - - - 89.6 89.3

(RON+MON)/2 - - 95.4 - 95.5 - - - 95.8 - - - - - - 95.5 95.6

C mass % D5291 mod.** 78.34 - - - 77.60 - - - - - - - 78.37 78.64 78.24

H mass % D5291 mod.** 13.76 - - - 13.87 - - - - - - - 14.05 13.71 13.85

O mass % D5599 - - 8.3 7.9 - - 7.7 - - - - 7.0 - 7.5 7.7

Net Heat of Combustion MJ/kg D4809 40.254 - - - - - 39.816 - - - - - - 40.022 40.031

Water mass % E-1064 - - - - - - 0.105 - - - - 0.121 - - 0.113

Lead g/l D3237 - - - - - - 0.004 - - - - - - - 0.004

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 23 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7473 0.7477 - 0.7477 0.7475 - - - - - - - - - 0.7476

API Gravity, 60oF

o

API D4052 57.6 57.5 - 57.6 57.6 - - - - - - - - - 57.6

Ethanol vol. % D5599 - - 21.77 21.03 - - 20.26 - - - - 18.50 - 20.04 20.32

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.1 - - <0.10

Distillation IBP oF 110.0 107.4 - - - 110.0 - - - 108.1 108.5 - - 110.1 109.0

5% evap oF 132.7 133.8 - - - 132.8 - - - 133.2 132.7 - - 134.3 133.3

10% evap oF 138.8 139.1 - - - 138.6 - - - 139.1 138.8 - - 139.1 138.9

20% evap oF 146.2 146.5 - - - 145.9 - - - 146.4 146.0 - - 146.1 146.2

30% evap oF 152.7 152.6 - - - 151.9 - - - 152.7 152.2 - - 151.9 152.3

40% evap oF 158.2 157.8 - - - 157.6 - - - 158.0 157.6 - - 157.4 157.8

50% evap oF 162.3 162.9 - - - 162.5 - - - 162.9 162.4 - - 162.2 162.5

60% evap oF 170.7 165.6 - - - 172.6 - - - 174.1 169.0 - - 177.7 171.6

70% evap oF 269.9 271.5 - - - 269.5 - - - 271.0 271.5 - - 271.9 270.9

80% evap oF 311.5 312.5 - - - 311.0 - - - 311.4 309.3 - - 312.5 311.4

90% evap oF 338.6 339.1 - - - 338.1 - - - 337.8 338.0 - - 337.7 338.2

95% evap oF 350.3 350.1 - - - 348.7 - - - 350.0 350.0 - - 350.8 350.0

FBP oF 365.6 367.0 - - - 365.2 - - - 359.6 365.2 - - 365.0 364.6

Recovery vol. % 97.9 98.3 - - - 98.4 - - - 98.0 97.9 - - 98.6 98.0

Residue vol. % 1.0 1.0 - - - 1.0 - - - 1.0 1.0 - - 1.0 1.0

Loss vol. % 1.1 0.7 - - - 0.6 - - - 1.0 1.1 - - 0.4 1.0

Corrected Recovery vol. % 98.1 98.3 - - - - - - - 98.0 98.1 - - - 98.1

Corrected Loss vol. % 0.9 0.7 - - - - - - - 1.0 0.9 - - - 0.9

DVPE (EPA equation) psi D5191 6.93 6.96 6.68 6.92 6.28 - 6.81 - - - 6.90 6.91 - 6.64 6.84

Aromatics vol. % D1319 - 16.3 - 15.4 16.2 16.6 - 15.5 - - - - 14.6 16.5 15.9

Olefins vol. % D1319 - 8.1 - 7.3 8.0 7.9 - 6.8 - - - - 7.1 7.0 7.5

Saturates vol. % * - - - - - - - - - - - - - - 56.4

Benzene vol. % D3606 - - - 0.58 - - 0.68 - - - - 0.55 - 0.70 0.63

S mg/kg D5453 20 23 19 20 - - 22 - - - - - - 22 21

RON - D2699 97.4 - 97.4 - - - 97.2 - - - - - - 97.7 97.4

MON - D2700 86.0 - 87.2 - - - 86.4 - - - - - - 87.4 86.8

(RON+MON)/2 - - 91.7 - 92.3 - - - 91.8 - - - - - - 92.6 92.1

C mass % D5291 mod.** 78.82 - - - 77.90 - - - - - - - 78.81 77.83 78.34

H mass % D5291 mod.** 13.82 - - - 13.79 - - - - - - - 13.97 14.88 13.86

O mass % D5599 - - 8.0 7.8 - - 7.5 - - - - 6.8 - 7.4 7.5

Net Heat of Combustion MJ/kg D4809 39.966 - - - - - 39.896 - - - - - - 39.882 39.915

Water mass % E-1064 - - - - - - - - - - - 0.112 - - 0.112

Lead g/l D3237 - - - - - - <0.003 - - - - - - - <0.003

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - 0.5 - - - - - - - 0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 24 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7419 0.7424 - 0.7423 0.7422 - - - - - - - - - 0.7422

API Gravity, 60oF

o

API D4052 59.0 58.9 - 58.9 58.9 - - - - - - - - - 58.9

Ethanol vol. % D5599 - - 22.2 21.17 - - 20.44 - - - - 18.68 - 20.08 20.51

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - 0.03 - - - - <0.1 - - <0.10

Distillation IBP oF 87.8 90.4 - - - 89.8 - - 91.2 90.7 89.8 - - 90.5 89.7

5% evap oF 116.8 117.3 - - - 114.0 - - 112.3 115.1 116.1 - - 119.5 115.9

10% evap oF 127.3 127.9 - - - 125.5 - - 124.1 127.0 127.0 - - 128.7 126.9

20% evap oF 143.3 143.4 - - - 141.7 - - 141.4 142.9 142.7 - - 143.5 142.8

30% evap oF 152.4 153.9 - - - 152.3 - - 152.5 153.6 153.7 - - 153.8 153.2

40% evap oF 160.5 160.9 - - - 159.7 - - 159.3 160.5 160.5 - - 160.2 160.4

50% evap oF 165.3 165.3 - - - 164.4 - - 163.9 165.5 165.1 - - 164.8 165.1

60% evap oF 171.8 171.3 - - - 174.2 - - 169.7 174.6 172.6 - - 184.9 172.9

70% evap oF 265.1 265.9 - - - 265.1 - - 262.8 267.0 267.2 - - 269.7 266.1

80% evap oF 305.8 306.3 - - - 303.6 - - 302.6 305.4 306.3 - - 309.6 305.5

90% evap oF 338.3 338.6 - - - 337.6 - - 336.1 337.9 338.1 - - 340.6 338.1

95% evap oF 350.6 350.3 - - - 349.8 - - 349.1 350.2 350.6 - - 353.6 350.3

FBP oF 369.5 371.7 - - - 366.0 - - 367.7 363.8 370.1 - - 370.0 368.2

Recovery vol. % 98.2 97.6 - - - 97.2 - - 96.4 97.3 97.4 - - 97.6 97.6

Residue vol. % 1.0 1.0 - - - 1.1 - - 1.1 1.0 1.1 - - 1.1 1.0

Loss vol. % 0.8 1.4 - - - 1.7 - - 2.5 1.7 1.5 - - 1.3 1.4

Corrected Recovery vol. % 98.3 97.7 - - - - - - - 97.3 97.6 - - - 97.7

Corrected Loss vol. % 0.7 1.3 - - - - - - - 1.7 1.3 - - - 1.3

DVPE (EPA equation) psi D5191 10.08 10.21 9.76 10.24 9.33 - 10.26 - - - 10.19 10.03 - 10.19 10.12

Aromatics vol. % D1319 - 14.5 - 15.2 15.9 15.9 - 14.6 - - - - - 15.9 15.3

Olefins vol. % D1319 - 7.5 - 6.2 9.0 7.0 - 7.4 - - - - - 6.6 7.3

Saturates vol. % * - - - - - - - - - - - - - - 56.9

Benzene vol. % D3606 - - - 0.62 - - 0.56 - - - - 0.57 - 0.71 0.62

S mg/kg D5453 20 24 20 20 - - 22 - - - - - - 21 21

RON - D2699 101.3 - 100.5 - - - 100.9 - - - - - - 100.5 100.8

MON - D2700 88.0 - 88.4 - - - 89.6 - - - - - - 88.5 88.6

(RON+MON)/2 - - 94.7 - 94.5 - - - 95.3 - - - - - - 94.5 94.7

C mass % D5291 mod.** 78.48 - - - 77.60 - - - - - - - 78.52 78.40 78.47

H mass % D5291 mod.** 13.74 - - - 13.76 - - - - - - - 14.00 13.94 13.86

O mass % D5599 - - 8.2 7.9 - - 7.6 - - - - 6.9 - 7.5 7.6

Net Heat of Combustion MJ/kg D4809 40.262 - - - - - - - - - - - - 39.966 40.114

Water mass % E-1064 - - - - - - 0.103 - - - - 0.113 - - 0.108

Lead g/l D3237 - - - - - - 0.005 - - - - - - - 0.005

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - 0.5 - - - - - - - 0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 25 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7698 0.7704 - 0.7702 0.7705 - - - - - - - - - 0.7702

API Gravity, 60oF

o

API D4052 52.1 52.0 - 52.0 52.0 - - - - - - - - - 52.0

Ethanol vol. % D5599 - - 21.02 20.52 - - 20.23 - - - - 18.49 - 19.91 20.03

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.1 - - <0.10

Distillation IBP oF 88.5 88.6 - - - 86.8 - - 88.3 90.4 90.7 - - 92.2 89.0

5% evap oF 114.1 115.0 - - - 110.2 - - 115.2 114.7 114.5 - - 119.2 113.7

10% evap oF 125.8 126.6 - - - 122.5 - - 126.3 126.5 126.3 - - 129.4 125.5

20% evap oF 142.2 142.9 - - - 140.5 - - 143.1 142.5 142.5 - - 145.1 142.1

30% evap oF 153.3 153.7 - - - 152.8 - - 154.0 153.5 153.3 - - 154.7 153.3

40% evap oF 161.2 161.3 - - - 160.5 - - 161.1 160.6 160.7 - - 161.8 160.9

50% evap oF 167.5 166.5 - - - 166.7 - - 167.5 166.8 166.8 - - 167.2 166.9

60% evap oF 191.1 193.9 - - - 187.3 - - 226.8 193.2 191.2 - - 237.4 191.3

70% evap oF 282.1 281.6 - - - 280.0 - - 284.7 283.2 280.9 - - 288.7 281.6

80% evap oF 310.5 312.0 - - - 309.9 - - 314.2 309.7 309.6 - - 316.8 310.3

90% evap oF 337.7 338.9 - - - 337.3 - - 342.1 337.7 337.8 - - 344.1 337.9

95% evap oF 353.5 352.9 - - - 352.8 - - 359.8 353.1 351.0 - - 362.7 352.7

FBP oF 371.7 375.0 - - - 371.5 - - 369.7 368.0 372.7 - - 376.9 371.8

Recovery vol. % 97.7 97.4 - - - 97.4 - - 97.1 97.2 97.1 - - 97.1 97.4

Residue vol. % 1.0 1.1 - - - 1.1 - - 1.1 1.1 1.1 - - 1.1 1.1

Loss vol. % 1.3 1.5 - - - 1.5 - - 1.8 1.7 1.8 - - 1.8 1.6

Corrected Recovery vol. % 97.9 97.4 - - - - - - - 97.1 97.4 - - - 97.5

Corrected Loss vol. % 1.1 1.5 - - - - - - - 1.8 1.5 - - - 1.5

DVPE (EPA equation) psi D5191 10.15 10.25 9.99 10.27 9.38 - 10.31 - - - 10.08 10.14 - 10.10 10.16

Aromatics vol. % D1319 - 35.2 - 35.1 35.4 36.0 - 35.4 - - - - 35.0 37.9 35.2

Olefins vol. % D1319 - 7.5 - 6.5 6.7 7.6 - 5.4 - - - - 5.8 6.8 6.6

Saturates vol. % * - - - - - - - - - - - - - - 38.1

Benzene vol. % D3606 - - - 0.63 - - 0.59 - - - - 0.60 0.69 0.75 0.65

S mg/kg D5453 24 29 24 25 - - 27 - - - - - - 25 25.7

RON - D2699 102.6 - 102.3 - - - 102.6 - - - - - - 101.3 102.2

MON - D2700 88.1 - 88.6 - - - 88.2 - - - - - - 88.4 88.3

(RON+MON)/2 - - 95.4 - 95.5 - - - 95.4 - - - - - - 94.9 95.3

C mass % D5291 mod.** 81.94 - - - 79.47 - - - - - - - 80.10 80.97 80.62

H mass % D5291 mod.** 12.46 - - - 12.55 - - - - - - - 12.66 11.85 12.38

O mass % D5599 - - 7.5 7.4 - - 7.3 - - - - 6.6 - 7.1 7.2

Net Heat of Combustion MJ/kg D4809 39.578 - - - - - 39.352 - - - - - - 37.634 38.855

Water mass % E-1064 - - - - - - 0.113 - - - - 0.120 - - 0.117

Lead g/l D3237 - - - - - - 0.001 - - - - - - - 0.001

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 26 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7589 0.7594 - 0.7595 0.7594 - - - - - - - - - 0.7593

API Gravity, 60oF

o

API D4052 54.7 54.6 - 54.6 54.6 - - - - - - - - - 54.6

Ethanol vol. % D5599 - - 15.97 15.85 - - 15.05 - - - - 14.19 - 15.13 15.24

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.1 - - <0.10

Distillation IBP oF 87.4 90.2 - - - 91.1 - - 85.7 89.0 88.6 - - 92.9 88.7

5% evap oF 110.3 110.4 - - - 109.3 - - 107.4 109.3 110.8 - - 113.3 109.6

10% evap oF 117.4 118.0 - - - 116.7 - - 115.6 116.9 117.9 - - 119.4 117.1

20% evap oF 128.3 128.6 - - - 127.5 - - 126.6 127.3 128.2 - - 129.7 127.8

30% evap oF 139.3 139.2 - - - 137.9 - - 137.6 138.7 139.0 - - 140.1 138.6

40% evap oF 150.5 150.0 - - - 149.2 - - 149.2 149.8 150.0 - - 151.3 149.8

50% evap oF 161.1 160.6 - - - 160.0 - - 159.7 159.7 160.4 - - 161.3 160.3

60% evap oF 177.5 176.4 - - - 175.6 - - 172.4 172.9 173.6 - - 188.0 174.7

70% evap oF 277.9 276.7 - - - 277.6 - - 275.7 276.5 277.3 - - 280.0 277.0

80% evap oF 307.4 308.3 - - - 307.6 - - 304.5 305.4 305.5 - - 312.7 306.5

90% evap oF 339.4 339.6 - - - 338.1 - - 338.1 338.4 338.5 - - 344.1 338.7

95% evap oF 357.3 357.4 - - - 357.1 - - 354.9 356.5 357.1 - - 357.1 356.7

FBP oF 376.0 378.4 - - - 379.6 - - 373.5 378.1 378.3 - - 376.4 377.3

Recovery vol. % 98.5 97.7 - - - 98.1 - - 98.0 98.0 98.0 - - 97.4 98.1

Residue vol. % 1.1 1.1 - - - 1.1 - - 1.1 1.1 1.1 - - 1.1 1.1

Loss vol. % 0.4 1.2 - - - 0.8 - - 0.9 0.9 0.9 - - 1.5 0.9

Corrected Recovery vol. % 98.5 97.7 - - - - - - - 98.0 98.1 - - - 98.1

Corrected Loss vol. % 0.4 1.2 - - - - - - - 0.9 0.8 - - - 0.8

DVPE (EPA equation) psi D5191 10.27 10.37 10.08 10.33 9.50 10.14 10.28 - - - 10.29 10.16 - 9.96 10.2

Aromatics vol. % D1319 - 35.1 - 35.6 34.7 37.3 - 35.4 - - - - 34.0 36.9 35.6

Olefins vol. % D1319 - 7.9 - 6.3 6.5 5.7 - 5.6 - - - - 6.5 6.8 6.5

Saturates vol. % * - - - - - - - - - - - - - - 42.7

Benzene vol. % D3606 - - - 0.60 - - 0.56 - - - - 0.59 0.69 0.67 0.62

S mg/kg D5453 22 26 21 22 - 24 22 - - - - - - 23 23

RON - D2699 102.4 - 101.7 - - - 101.6 - - - - - - 101.1 101.7

MON - D2700 88.3 - 88.9 - - - 88.0 - - - - - - 88.8 88.5

(RON+MON)/2 - - 95.4 - 95.3 - - - 94.8 - - - - - - 95.0 95.1

C mass % D5291 mod.** 81.6 - - - 80.57 - - - - - - - 81.66 82.09 81.48

H mass % D5291 mod.** 12.35 - - - 12.44 - - - - - - - 12.83 12.18 12.45

O mass % D5599 - - 5.8 5.8 - - 5.5 - - - - 5.2 - 5.5 5.6

Net Heat of Combustion MJ/kg D4809 40.586 - - - - - 40.122 - - - - - - 40.444 40.384

Water mass % E-1064 - - - - - - 0.084 - - - - 0.091 - - 0.088

Lead g/l D3237 - - - - - - <0.003 - - - - - - - <0.003

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 27 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7432 0.7435 - 0.7435 0.7433 - - - - - - - - - 0.7434

API Gravity, 60oF

o

API D4052 58.6 58.6 - 58.6 58.7 - - - - - - - - - 58.6

Ethanol vol. % D5599 - - 15.99 15.09 - - 15.15 - - - - 14.18 14.31 14.71 14.91

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.1 0.09 - <0.10

Distillation IBP oF 104.5 102.4 - - - 104.7 - - 101.5 105.9 103.7 - - 110.6 104.8

5% evap oF 135.1 136.3 - - - 132.3 - - 134.5 134.7 136.6 - - 137.6 135.3

10% evap oF 142.5 142.5 - - - 141.2 - - 141.7 142.3 143.0 - - 143.1 142.3

20% evap oF 152.1 152.4 - - - 151.4 - - 151.5 152.1 151.8 - - 152.7 152.0

30% evap oF 158.8 158.5 - - - 158.2 - - 155.0 158.6 158.4 - - 158.7 158.0

40% evap oF 164.0 164.6 - - - 163.3 - - 163.0 164.1 163.3 - - 164.1 163.8

50% evap oF 219.7 221.6 - - - 218.1 - - 223.6 219.7 222.4 - - 225.3 221.5

60% evap oF 249.9 249.9 - - - 351.1 - - 250.5 250.8 251.6 - - 252.0 265.1

70% evap oF 273.5 275.2 - - - 274.2 - - 276.6 274.4 274.6 - - 275.8 274.9

80% evap oF 310.5 310.4 - - - 309.6 - - 312.5 309.6 310.8 - - 315.9 311.3

90% evap oF 340.1 339.3 - - - 339.3 - - 341.4 340.0 340.2 - - 342.1 340.3

95% evap oF 351.4 352.3 - - - 351.0 - - 354.4 350.8 351.6 - - 351.8 351.9

FBP oF 373.7 374.3 - - - 373.7 - - 368.0 367.0 376.2 - - 372.4 372.2

Recovery vol. % 98.3 98.3 - - - 97.6 - - 97.7 97.6 98.3 - - 97.5 98.1

Residue vol. % 1.0 1.0 - - - 1.0 - - 1.0 1.0 1.0 - - 1.0 1.0

Loss vol. % 0.7 0.7 - - - 1.4 - - 1.3 1.4 0.7 - - 1.5 0.9

Corrected Recovery vol. % 98.3 98.3 - - - - - - - 97.6 98.3 - - - 98.1

Corrected Loss vol. % 0.7 0.7 - - - - - - - 1.4 0.7 - - - 0.9

DVPE (EPA equation) psi D5191 7.01 7.03 6.87 6.99 6.35 6.90 7.04 - - - 7.00 7.01 - 6.92 6.97

Aromatics vol. % D1319 - 14.6 - 14.9 15.3 14.6 - 14.1 - - - - 14.3 16.2 14.9

Olefins vol. % D1319 - 8.0 - 7.2 7.2 7.7 - 6.0 - - - - 7.5 8.1 7.4

Saturates vol. % * - - - - - - - - - - - - - - 62.9

Benzene vol. % D3606 - - - 0.57 - - 0.53 - - - - 0.54 0.51 0.66 0.56

S mg/kg D5453 25 28 24 26 - - 26 - - - - - - 26 26

RON - D2699 101.6 - 100.5 - - - 100.7 - - - - - - 100.2 100.8

MON - D2700 88.8 - 89.6 - - - 89.1 - - - - - - 89.4 89.2

(RON+MON)/2 - - 95.2 95.1 - - - 94.9 - - - - - - 94.8 95.0

C mass % D5291 mod.** 80.05 - - - 79.54 - - - - - - - 80.41 81.08 80.27

H mass % D5291 mod.** 13.96 - - - 14.05 - - - - - - - 14.19 13.85 14.01

O mass % D5599 - - 5.9 5.6 - - 5.6 - - - - 5.3 5.3 5.5 5.5

Net Heat of Combustion MJ/kg D4809 41.200 - - - - - 40.830 - - - - - - 41.156 41.062

Water mass % E-1064 - - - - - - 0.088 - - - - 0.091 - - 0.090

Lead g/l D3237 - - - - - - <0.003 - - - - - - - <0.003

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - 0.5 - - - - - - - 0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 28 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7697 0.7701 - 0.7700 0.7699 - - - - - - - - - 0.7699

API Gravity, 60oF

o

API D4052 52.1 52.1 - 52.1 52.1 - - - - - - - - - 52.1

Ethanol vol. % D5599 - - 15.50 15.73 - - 14.96 - - - - 14.41 14.67 14.59 14.98

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.1 0.09 - <0.10

Distillation IBP oF 104.5 104.5 - - - 105.6 - - 100.6 104.8 103.2 - - 107.4 103.9

5% evap oF 136.7 138.0 - - - 133.8 - - 135.4 137.0 137.0 - - 136.1 136.3

10% evap oF 144.6 144.9 - - - 142.9 - - 143.5 144.6 144.8 - - 143.6 144.2

20% evap oF 154.3 154.3 - - - 153.3 - - 153.7 154.0 154.2 - - 153.0 154.0

30% evap oF 160.6 160.5 - - - 160.0 - - 159.2 160.8 160.0 - - 159.0 160.2

40% evap oF 167.3 165.4 - - - 166.5 - - 162.6 167.5 165.7 - - 164.3 165.8

50% evap oF 216.7 215.8 - - - 215.9 - - 216.9 216.6 217.7 - - 219.2 216.6

60% evap oF 239.7 240.2 - - - 240.1 - - 237.8 241.2 242.0 - - 241.3 240.2

70% evap oF 249.0 254 - - - 253.2 - - 247.3 253.2 252.6 - - 253.9 251.6

80% evap oF 269.1 269.1 - - - 268.0 - - 267.7 268.2 268.3 - - 270.3 268.4

90% evap oF 298.9 299.4 - - - 298.6 - - 298.4 298.0 299.5 - - 303.2 298.8

95% evap oF 328.4 327.3 - - - 327.5 - - 326.0 326.5 327.8 - - 336.5 327.3

FBP oF 363.8 366.3 - - - 362.8 - - 362.4 359.1 364.5 - - 364.3 363.2

Recovery vol. % 98.3 98.2 - - - 97.7 - - 98.5 98.2 98.3 - - 98.2 98.3

Residue vol. % 1.0 1.0 - - - 1.0 - - 1.0 1.0 1.0 - - 1.0 1.0

Loss vol. % 0.7 0.8 - - - 1.3 - - 0.5 0.8 0.7 - - 0.8 0.8

Corrected Recovery vol. % 98.3 98.2 - - - - - - - 98.2 98.4 - - - 98.3

Corrected Loss vol. % 0.7 0.8 - - - - - - - 0.8 0.7 - - - 0.8

DVPE (EPA equation) psi D5191 6.92 6.93 6.77 6.92 6.20 - 6.93 - - - 6.83 6.83 - 6.80 6.87

Aromatics vol. % D1319 - 34.6 - 34.5 34.1 34.6 - 33.7 - - - - 33.4 36.5 34.5

Olefins vol. % D1319 - 8.4 - 6.6 7.3 6.9 - 5.4 - - - - 7.1 7.2 7.0

Saturates vol. % * - - - - - - - - - - - - - - 43.5

Benzene vol. % D3606 - - - 0.57 - - 0.54 - - - - 0.55 0.59 0.69 0.59

S mg/kg D5453 22 26 22 24 - - 24 - - - - - - 24 24

RON - D2699 103.2 - 102.9 - - - 102.8 - - - - - - 101.8 102.7

MON - D2700 89.0 - 89.8 - - - 88.9 - - - - - - 89.8 89.4

(RON+MON)/2 - - 96.1 - 96.4 - - - 95.9 - - - - - - 95.8 96.1

C mass % D5291 mod.** 82.17 - - - 81.02 - - - - - - - 81.86 82.05 81.78

H mass % D5291 mod.** 12.58 - - - 12.60 - - - - - - - 12.79 12.50 12.62

O mass % D5599 - - 5.5 5.6 - - 5.4 - - - - 5.2 5.3 5.2 5.4

Net Heat of Combustion MJ/kg D4809 40.442 - - - - - 40.180 - - - - - - 40.528 40.383

Water mass % E-1064 - - - - - - 0.088 - - - - 0.094 - - 0.091

Lead g/l D3237 - - - - - - <0.003 - - - - - - - <0.003

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

Average TEST 

METHOD PROPERTY UNIT

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 29 Red fill color indicates an outlier Orange fill color indicates data not included in parameter averages

Lab A Lab B Lab C Lab D Lab E F G H I J K L M N O

Density, 60oF g/cm3 D4052 0.7797 0.7800 0.7818 0.7829 0.7788 - - - 0.7798 0.7798 - - - 0.7799 - 0.7797

API Gravity, 60oF

o

API D4052 49.8 49.7 49.3 49.1 49.8 - - - 49.8 49.8 - - - 49.8 - 49.8

Uncorrected Ethanol mass % D5501 mod.* - - 80.28 - - - - - - - 78.90 - - - - 79.59

Uncorrected Methanol mass % D5501 mod.* - - - - - - - - - - 0.01 - - - - 0.01

Ethanol vol. % D5501 mod.* 75.80 - 78.51 77.39 - - - - - - 76.88 - - 76.24*** - 77.15

Methanol vol. % D5501 mod.* Not 

detected

Not 

detected

Not 

detected

Not 

detected

Not 

detected - - - - - <0.01 - - 0.62*** - <0.01

Estimated Hydrocarbon 

Content vol. % 100 - D5501Ethanol - E203Water 23.57 - 20.69 21.91 - - - - - - 22.40 - - 23.04*** - 22.14

Distillation IBP oF 105.1 92.3 109.0 102.1 102.0 - - 105.1 99.5 - 95.3 94.9 90.6 102.6 - 99.0

5% evap oF 123.6 132.1 135.1 135.6 135.5 - - 129.6 127.7 - 132.4 136.3 132.6 143.6 - 132.9

10% evap oF 147.3 153.7 158.0 156.4 154.9 - - 151.3 154.0 - 155.6 156.0 155.1 158.6 - 154.3

20% evap oF 165.6 168.2 170.4 167.6 167.4 - - 167.2 168.7 - 168.7 167.5 167.5 168.0 - 167.6

30% evap oF 169.4 170.8 172.7 170.0 169.9 - - 170.2 171.3 - 171.2 170.0 170.0 170.2 - 170.3

40% evap oF 170.5 171.7 173.8 170.8 170.8 - - 171.3 172.2 - 172.1 170.9 170.9 171.1 - 171.2

50% evap oF 171.2 172.1 174.3 171.3 171.3 - - 171.9 172.6 - 172.7 171.6 171.4 171.4 - 171.8

60% evap oF 171.6 172.5 174.7 171.7 171.7 - - 172.2 173.0 - 173.0 171.9 171.8 171.9 - 172.1

70% evap oF 172.0 172.8 175.1 172.2 172.0 - - 172.6 173.4 - 173.4 172.2 172.2 172.3 - 172.5

80% evap oF 172.5 173.2 175.4 172.4 172.4 - - 172.9 173.7 - 173.6 172.6 172.6 172.7 - 172.9

90% evap oF 173.6 174.1 176.1 173.9 173.3 - - 173.8 174.5 - 174.7 173.6 173.7 173.7 - 173.9

95% evap oF 175.4 176.1 177.9 177.6 175.5 - - 175.8 176.3 - 176.9 175.9 176.0 176.1 - 176.2

FBP oF 180.6 269.9 181.9 180.6 299.1 - - 298.2 263.5 - 294.5 286.9 292.0 292.8 - 265.8

Recovery vol. % 96.3 98.0 95.9 95.6 98.5 - - 98.6 97.6 - 98.3 97.4 97.6 99.1 - 98.1

Residue vol. % 1.6 1.1 1.7 1.6 0.8 - - 0.9 0.6 - 0.6 0.9 0.9 0.9 - 0.8

Loss vol. % 2.2 0.8 2.4 2.8 0.7 - - 0.5 1.8 - 1.1 1.7 1.5 0 - 1.1

Corrected Recovery vol. % - - - - - - - 98.6 98.0 - 98.5 97.3 97.7 99.0 - 98.2

Corrected Loss vol. % - - - - - - - 0.5 1.4 - 0.9 1.8 1.4 0.1 - 1.0

DVPE (EPA equation) psi D5191 9.01 9.04 8.76 7.72 9.02 - - 8.58 9.05 8.12 9.07 - 8.86 - - 8.92

Benzene vol. % D5580 - - - - - - - 0.12 - - - - - - 0.12

S mg/kg D5453 - - - - - - 18 - 16 - - - - 14 - 16

C mass % D5291 mod.** - - - - - 57.88 - - - 57.66 - - - 57.04 58.39 57.74

H mass % D5291 mod.** - - - - - 13.1 - - - 12.08 - - - 13.08 12.92 12.80

O mass % D5501 mod.* 26.76 - 27.65 27.21 - - - - - - 27.15 - - 27.03*** - 27.19

mass % E203 0.81 0.96 1.03 0.90 0.95 - - - - - - - - 0.91 - 0.93

vol. % E203 0.63 0.75 0.80 0.70 0.74 - - - - - - - - 0.71 - 0.72

Net Heat of Combustion MJ/kg D4809 30.058 - - - - - - - - - 30.058

Solvent Washed Gum mg/100 ml D381 - - - - - 2.8 1.0 - - - - - - - - 1.9

Unwashed Gum mg/100 ml D381 - - - - - 0.6 3.0 - - - - - - - - 1.8

Acidity (as acetic acid) mass % D1613 - - - - - - 0.0021 - - - - - - - - 0.0021

pHe - D6423 - - - - - - 7.96 - - - 8.20 - - - - 8.08

Inorganic Chloride mg/kg D7319 - - - - - -

Not 

detected - - - - - - - - Not detected

Copper mg/l D1688 modified as 

outlined in D4806 - - - - - - 0.02 - - - - - - - - 0.02

* Method adapted by individual laboratories to testing of E85 fuels

** Method adapted by individual laboratories to testing of gasolines

*** Data not included in parameter averages due to suspected sample contamination with methanol

Water

TEST METHOD Average

Data From 2008 CRC E85 Class Volatility Program Round Robin Participant

PROPERTY UNIT

D86 (non-OptiDist)
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 30 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7505 0.7509 - 0.7509 0.7508 - - - - - - - - - 0.7508

API Gravity, 60oF

o

API D4052 56.8 56.8 - 56.8 56.8 - - - - - - - - - 56.8

Ethanol vol. % D5599 - - 10.69 9.88 - - 9.74 - - - - 9.86 9.67 9.91 9.8

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.1 0.07 - <0.10

Distillation IBP oF 91.9 91.0 - - - 92.4 - - 90.3 88.2 91.6 - - 92.0 90.9

5% evap oF 110.9 110.4 - - - 109.8 - - 110.8 109.7 110.4 - - 108.0 110.3

10% evap oF 117.0 117.1 - - - 116.1 - - 116.6 116.4 116.9 - - 115.0 116.7

20% evap oF 125.4 126.1 - - - 124.7 - - 125.4 125.3 125.2 - - 125.0 125.4

30% evap oF 134.4 134.5 - - - 132.2 - - 134.1 134.0 133.9 - - 134.0 133.9

40% evap oF 143.4 143.6 - - - 142.6 - - 142.9 143.2 143.1 - - 143.0 143.1

50% evap oF 153.4 153.6 - - - 152.8 - - 151.7 152.9 153.0 - - 152.0 152.9

60% evap oF 196.8 197.2 - - - 196.4 - - 200.7 196.7 195.5 - - 208.0 197.2

70% evap oF 266.8 267.2 - - - 267.9 - - 268.3 266.7 266.7 - - 270.0 267.3

80% evap oF 295.4 295.7 - - - 294.1 - - 294.4 294.2 293.9 - - 298.0 294.6

90% evap oF 324.3 323.5 - - - 323.9 - - 324.1 323.4 323.6 - - 329.0 323.8

95% evap oF 341.9 341.8 - - - 341.4 - - 341.6 341.7 342.5 - - 333.0 341.8

FBP oF 366.5 368.7 - - - 366.4 - - 363.6 362.7 368.6 - - 364.0 366.1

Recovery vol. % 98.2 97.7 - - - 98.1 - - 97.9 98.1 97.8 - - 97.2 98.0

Residue vol. % 1.0 1.0 - - - 1.0 - - 1.0 1.0 1.0 - - 1.0 1.0

Loss vol. % 0.8 1.3 - - - 0.9 - - 1.1 0.9 1.2 - - 1.8 1.1

Corrected Recovery vol. % 98.3 97.7 - - - - - - - 98.0 98.0 - - - 98.0

Corrected Loss vol. % 0.7 1.3 - - - - - - - 1.0 1.0 - - - 1.0

DVPE (EPA equation) psi D5191 10.27 10.28 10.15 10.33 9.44 10.25 10.37 - - - 10.26 10.08 - 10.04 10.23

Aromatics vol. % D1319 - 33.9 - 35.6 34.5 36.0 - 34.1 - - - - 37.4 37.1 35.5

Olefins vol. % D1319 - 6.8 - 5.7 6.7 6.2 - 5.7 - - - - 7.7 6.4 6.5

Saturates vol. % * - - - - - - - - - - - - - - 48.2

Benzene vol. % D3606 - - - 0.58 - - 0.53 - - - - 0.56 0.53 0.70 0.58

S mg/kg D5453 21 25 21 21 - - 24 - - - - - - 25 23

RON - D2699 101.3 - 100.5 - - - 100.5 - - - - - - 100.4 100.5

MON - D2700 87.8 - 88.7 - - - 87.6 - - - - - - 88.3 88.1

(RON+MON)/2 - - 94.6 - 94.6 - - - 94.1 - - - - - - 94.4 94.3

C mass % D5291 mod.** 83.78 - - - 82.64 - - - - - - - 83.58 82.66 83.17

H mass % D5291 mod.** 12.36 - - - 12.88 - - - - - - - 12.93 13.83 13.00

O mass % D5599 - - 3.9 3.6 - - 3.6 - - - - 3.6 3.6 3.7 3.6

Net Heat of Combustion MJ/kg D4809 41.474 - - - - - 41.088 - - - - - - 41.350 41.304

Water mass % E-1064 - - - - - - - - - - - 0.086 - - 0.086

Lead g/l D3237 - - - - - - - - - - - - - - -

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - <0.5 - - - - - - - <0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

D86 (OptiDist 

or equivalent)

PROPERTY UNIT Average TEST 

METHOD

Laboratory
Phase 3 of EPAct/V2/E-89 Program

Fuel Inspection Data

Fuel : 31 Red fill color indicates an outlier

1 2 3 4 5 6 7 8 9 10 11 12 13 14

Density, 60oF g/cm3 D4052 0.7739 0.7744 - 0.7743 0.7742 - - - - - - - - - 0.7742

API Gravity, 60oF

o

API D4052 51.1 51.0 - 51.1 51.1 - - - - - - - - - 51.1

Ethanol vol. % D5599 - - 20.86 20.95 - - 20.19 - - - - 18.45 - 20.08 20.11

Total Content of 

Oxygenates Other Than 

Ethanol

vol. % D5599 - - - - - - <0.01 - - - - <0.1 - - <0.10

Distillation IBP oF 104.0 105.9 - - - 109.7 - - - 103.1 106.1 - - 106.3 105.8

5% evap oF 132.3 133.8 - - - 133.3 - - - 131.5 131.7 - - 133.8 132.5

10% evap oF 139.0 139.8 - - - 139.5 - - - 138.7 138.5 - - 139.5 139.1

20% evap oF 147.8 148.2 - - - 147.8 - - - 147.5 147.2 - - 148.6 147.7

30% evap oF 155.3 155.5 - - - 154.9 - - - 154.9 154.7 - - 155.9 155.1

40% evap oF 161.8 161.1 - - - 161.5 - - - 161.2 161.1 - - 162.1 161.3

50% evap oF 167.6 167.9 - - - 167.4 - - - 167.3 166.4 - - 166.8 167.3

60% evap oF 215.4 218.5 - - - 210.8 - - - 214.2 210.9 - - 236.1 214.0

70% evap oF 270.5 273.5 - - - 270.3 - - - 272.3 271.3 - - 274.0 271.6

80% evap oF 297.7 298.7 - - - 297.2 - - - 296.4 294.8 - - 301.8 297.0

90% evap oF 325.6 325.6 - - - 324.6 - - - 325.0 325.1 - - 329.6 325.2

95% evap oF 342.5 343.5 - - - 341.7 - - - 340.8 342.1 - - 349.6 342.1

FBP oF 365.2 366.5 - - - 365.8 - - - 362.9 367.5 - - 366.0 365.6

Recovery vol. % 98.5 98.8 - - - 98.4 - - - 97.9 97.9 - - 97.6 98.3

Residue vol. % 1.0 1.0 - - - 1.0 - - - 1.0 1.0 - - 1.0 1.0

Loss vol. % 0.5 0.2 - - - 0.6 - - - 1.1 1.1 - - 1.4 0.7

Corrected Recovery vol. % 98.5 98.8 - - - - - - - 97.9 98.1 - - - 98.3

Corrected Loss vol. % 0.5 0.2 - - - - - - - 1.1 0.9 - - - 0.7

DVPE (EPA equation) psi D5191 7.05 7.07 6.92 7.05 6.25 - 6.98 - - - 7.00 6.88 - 6.88 6.98

Aromatics vol. % D1319 - 35.6 - 35.4 35.8 37.0 - 35.4 - - - - 35.4 38.0 35.5

Olefins vol. % D1319 - 8.4 - 6.6 6.5 6.8 - 5.8. - - - - 6.7 5.7 6.8

Saturates vol. % * - - - - - - - - - - - - - - 37.6

Benzene vol. % D3606 - - - 0.61 - - 0.60 - - - - 0.60 0.60 0.79 0.60

S mg/kg D5453 24 28 24 26 - - 27 - - - - - - 22 25

RON - D2699 102.4 - 101.8 - - - 101.9 - - - - - - 100.7 101.7

MON - D2700 87.8 - 88.7 - - - 88.0 - - - - - - 88.1 88.2

(RON+MON)/2 - - 95.1 - 95.3 - - - 95.0 - - - - - - 94.4 95.0

C mass % D5291 mod.** 79.94 - - - 79.12 - - - - - - - 80.14 80.41 79.90

H mass % D5291 mod.** 12.36 - - - 12.51 - - - - - - - 12.65 12.45 12.49

O mass % D5599 - - 7.4 7.5 - - 7.2 - - - - 6.6 - 7.2 7.2

Net Heat of Combustion MJ/kg D4809 39.702 - - - - - 39.204 - - - - - - 39.266 39.391

Water mass % E-1064 - - - - - - - - - - - 0.143 - - 0.143

Lead g/l D3237 - - - - - - <0.003 - - - - - - - <0.003

Copper Strip Corrosion - D130 - - - - - - 1A - - - - - - - 1A

Solvent Washed Gum mg/100ml D381 - - - - - - 0.5 - - - - - - - 0.5

Oxidation Stability min. D525 - - - - - - >240 - - - - - - - >240

* Calculated using the following equation: Saturates = 100 - D1319Aromatics - D1319Olefins - D5599Ethanol

** Method adapted by individual laboratories to testing of gasolines

PROPERTY UNIT Average

Laboratory

D86 (OptiDist 

or equivalent)

TEST 

METHOD