METHOD FOR PRODUCING STAGE-3 REFERENCE FUEL

Description

FIELD OF THE DISCLOSURE

[0001] This disclosure relates to the preparation of Tier 3 reference fuels.BACKGROUND OF THE DISCLOSURE

[0002] In an effort to further reduce motor vehicle emissions and improve air quality and public health, the United States Environmental Protection Agency has promulgated new rules that require lowering of sulfur content in gasoline beginning in 2017, and reduction of evaporative emissions from passenger cars, light-duty trucks, medium-duty passenger vehicles, and some heavyduty vehicles (40 CFR parts 79, 80, 85 et al., titled "Control of Air Pollution from Motor Vehicles: Tier 3 Motor Vehicle Emission and Fuel Standards; Final Rule). Under the Tier 3 program, gasoline shall not contain more than 10 parts per million sulfur on an annual average basis by January 1, 2017. This reduction is expected to reduce catalyst fouling and substantially improve the effectiveness of the vehicle emission control systems, leading to significant reductions in emissions of nitrogen oxides, volatile organic compounds, carbon monoxide, particulate matter, benzene, sulfur dioxide, 1,3-butadiene, formaldehyde, acetaldehyde, acrolein, and ethanol.

[0003] Under the Tier 3 standards, new specifications for the gasoline emissions test fuel used for testing highway vehicles have been adopted to better match the fuel that is currently being used. Specifically, in-use gasoline has changed considerably since the EPA last revised specifications for gasoline. Sulfur and benzene levels have been reduced, and gasoline containing 10 percent ethanol by volume has replaced non-oxygenated gasoline across the country. Section 1065.710(b) of Title 40 of the Code of Federal Regulations specifies test fuel properties for gasoline with ethanol (low-level blend only). The specification requires an Antiknock Index (R+M) / 2 of 87.0 - 88.4, a sensitivity (R-M) of 7.5 (minimum), a Dry Vapor Pressure Equivalent (DVPE) in units of kPa of 60.0 - 63.4, 10% evaporation during distillation at 49-60°C, 50% evaporation during distillation at 88-99°C, 90% evaporation during distillation at 157-168°C, a final boiling point of 193-216°C, a post-distillation residue of 2.0 milliliters (maximum) of a 100 milliliter specimen (see ASTM D86), total aromatic hydrocarbons content of 21.0-25.0 volume present, C6 aromatics (benzene) content of 0.5-0.7 volume percent, C7 aromatics (toluene) content of 5.2-6.4 volume percent, C8 aromatics content of 5.2-6.4 volume percent, C9 aromatics content of 5.2-6.4 volume percent, C10 plus aromatics content of 4.4-5.6 volume percent, a total olefins content of 4.0-10.0 mass percent, an ethanol content of 9.6-10.0 volume percent (blended) or 9.4-10.2 volume percent (confirmatory), a total content of oxygenates other than ethanol of 0.1 volume percent (maximum), a sulfur content of 8.0-11.0 mg / kg, a lead content of 0.0026 g / liter (maximum), a phosphorus content of 0.0013 g / liter (maximum), copper corrosion of No. 1 Maximum per ASTM D130, a solvent-washed gum content of 3.0 mg / 100 milliliters (maximum), and an oxidation stability of 1000 minutes (minimum) per ASTM D525. The ethanol (blended) specification is based on the volume percent ethanol content as determined during blending by the fuel supplier and as stated by the supplier at the time of fuel delivery (see 40 CFR 1065.710(b)(3)). The ethanol (confirmatory) specification refers to the volume percent ethanol content as determined analytically.

[0004] Section 1065.710 of Title 40 also specifies that the low-level ethanol-gasoline test fuel blend having nominally 10% ethanol (commonly called "E10 test fuel") must be prepared from typical refinery gasoline blending component, and "may not use pure compounds, except as follows: (i) you may use neat ethanol as a blendstock, (ii) you may adjust the test fuel's vapor pressure by adding butane, (iii) you may adjust the test fuel's benzene content by adding benzene, and (iv) you may adjust the test fuel's sulfur content by adding sulfur compounds that are representative of those found with in-use fuels."

[0005] As described in Dabelstein, Werner, et al., "Automative Fuels", in Ullmann's Encyclopedia of Industrial Chemistry, 2007, it is generally known that fuel requirements are fulfilled in refineries by use of available product streams. US 2015 / 0007489 A1 describes methods for providing liquid fuel compositions.

[0006] It has been determined that it is extremely difficult to meet all of the antiknock, sensitivity, distillation, and compositional requirements of 40 USC § 1065.710(b) using typical refinery gasoline blending components in combination with neat ethanol, butane, benzene and representative sulfur compounds. Generally, substantial trial and error is required to achieve all specifications concurrently. Further, once an appropriate blend has been determined, it is only usable for a relatively short period of time, since typical refinery gasoline blending components are constantly changing due to factors such as the source of the crude oil and seasonal adjustments to refinery operating parameters. It is most difficult to formulate an E10 test fuel within the specification having the required ranges for the various aromatic species while also meeting the total aromatic content and fuel distillation profile. Typical refinery gasoline blending components (or blendstocks) having a high aromatic content include heavy straight run (HSR) naphtha (petroleum), Aromatic 100 (a composition generally comprising a minimum of 98.0 volume percent aromatics and having a flashpoint of about 100 degrees Fahrenheit), Aromatic 150 (a composition generally comprising a minimum of 98.0 volume percent aromatics and having a flashpoint of about 150 degrees Fahrenheit), and Aromatic 200 (a composition generally comprising a minimum of 98.0 volume percent aromatics and having a flashpoint of about 200 degrees Fahrenheit). A problem with these aromatic refinery streams is that the composition can vary widely from batch to batch. Specifically, the distribution of C7, C8, C9 and C10+ aromatics can vary considerably from batch to batch, making it very difficult to formulate a finished test fuel meeting the very tight specifications of 40 CFR 1065.710(b). It is particularly difficult to formulate an E10 test fuel in accordance with 40 CFR 1065.710(b) that complies with the various aromatic species ranges while also meeting the total aromatic content requirement and fuel distillation profile.

[0007] It is highly desirable to develop a process for preparing E10 test fuels in accordance with 40 CFR 1065.710(b) without employing a trial and error process typically requiring several iterative failures before meeting all specifications.SUMMARY OF THE DISCLOSURE

[0008] The invention is defined by the appended claims. A process for preparing E10 test fuel in accordance with 40 CFR 1065.710(b) is described. The process includes steps of: (1) providing an aromatic pre-blend prepared by mixing an aromatic refinery blendstocks to obtain a mixture comprising aromatic compounds in proportions as specified in 40 CFR 1065.710(b); (2) combining the aromatic pre-blend with ethanol and at least one paraffinic refinery blendstock to obtain a composition complying with most of the compositional, fuel quality, and distillation profile requirements of 40 CFR 1065.710(b); and (3) adding butane as needed to adjust vapor pressure in accordance with 40 CFR 1065.710(b), optionally adding sulfur containing blendstock(s) or sulfur compounds as needed to comply with 40 CFR 1065.710(b), and optionally adding olefin containing blendstock(s) as needed to comply with 40 CFR 1065.710(b).

[0009] Alternatively, not according to the present invention, a process for preparing E10 test fuel in accordance with 40 CFR 1065.710(b) may comprise mixing (blending) aromatic refinery blendstocks with at least one paraffinic refinery blendstock, wherein the aromatic refinery blendstocks are selected such that if blended together without the at least one paraffinic refinery blendstock the resulting aromatic refinery blendstock mixture would comprise aromatic compounds in proportions as specified in 40 CFR 1065.710(b). Such alternative process may further comprise optionally adding butane as needed to adjust vapor pressure in accordance with 40 CFR 1065.710(b), optionally adding sulfur-containing blendstocks or sulfur compounds as needed to comply with 40 CFR 1065,710(b), and optionally adding olefin-containing blendstock(s) as needed to comply with 40 CFR 1065.710(b).

[0010] Also described is an aromatic pre-blend useful for preparing an E10 test fuel in accordance with 40 CFR 1065.710(b) by mixing it with a paraffinic refinery blendstock and optionally sulfur compound(s) and / or sulfur-containing blendstock(s), olefin-containing blendstock(s) and / or butane.

[0011] Other features and advantages of the present disclosure will become readily appreciated as the same becomes better understood after reading the following description.DETAILED DESCRIPTION

[0012] It has been discovered that it is possible to substantially reduce, and typically eliminate, trial and error during preparation of E10 test fuel in accordance with 40 CFR 1065.710(b) by first preparing an aromatic pre-blend having the required proportions of C6, C7, C8, C9 and C10+ aromatics, then combining the aromatic pre-blend with ethanol and a paraffinic refinery blendstock (refinery process stream) having a low aromatic content in proportions that are expected to provide the required ethanol and total aromatic content and distribution of 40 CFR 1065.710(b), and which is expected to provide the required distillation profile, antiknock index, sensitivity, lead content, phosphorus content, copper corrosion characteristic, solvent-washed gum content, and oxidation stability. Thereafter, small amounts of butane are added as needed to adjust the fuel vapor pressure, small amounts of sulfur-containing blendstock(s) representative of those found with in-use fuels are added to raise the sulfur content to that required by 40 CFR 1065.710(b), and a small amount of olefin-containing blendstock(s) is added to adjust the olefin content within the range required by 40 CFR 1065.710(b).

[0013] By properly adjusting the proportions of C6, C7, C8, C9 and C10+ aromatics in the pre-blend and combining the pre-blend with other blendstocks that do not have sufficiently high aromatic content to cause the C6-C10+ proportions in the combination to deviate substantially from that of the pre-blend, it is possible to meet all specification requirements without trial and error, or at least significantly reduce trial and error. In order to reduce or eliminate trial and error, it is desirable that the aromatic pre-blend is comprised of a very high proportion of aromatic compounds, such as at least 90 volume percent, at least 95 volume percent, or at least 98 volume percent. It is also desirable that the C6-C10+ proportions are as recited in 40 CFR 1065.710(b) (as published April 28, 2014 at 79 FR 23809). Specifically, it is desirable that the C7: C6, C8:C6 and C9:C6 aromatic proportions are each in the range 5.2-6.4:0.5-0.7 (in units of volume), and that the C10+:C6 aromatic proportion is in the range 4.4-5.6:0.5-0.7 (in units of volume).

[0014] The paraffinic refinery blendstock (or blendstocks) should be selected such that when it is combined with ethanol and the aromatic pre-blend to provide a 10% ethanol gasoline (E10 test fuel), the resulting mixture has the distillation profile and other fuel characteristics specified in 40 CFR 1065.710(b). The paraffinic blendstock or combination of paraffinic blendstocks should have a low aromatics content such that the distribution of aromatics in the blendstock(s) does not cause the C6-C10+ proportions in the test fuel to vary significantly from the proportions in the pre-blend. It is recommended that the aromatic content of the refinery blendstock or combination of refinery blendstocks that are mixed with the aromatic pre-blend and the ethanol does not exceed 10 volume percent, 5 volume percent, or 2 volume percent. The ethanol can be pure, or substantially pure, e.g., at least 90 volume percent ethanol, at least 95 volume percent ethanol, or at least 96 volume percent ethanol.

[0015] Suitable aromatic refinery blendstocks that are used for preparing the aromatic pre-blend include Aromatic-100, Aromatic-150, Aromatic-200, benzene, toluene, xylene (e.g., a mixture of o-, p- and m-xylene), 1,2,4-trimethyl benzene, 1,3,5-trimethyl benzene, diethylbenzene, and tetralin. Alternatively, not according to the invention, other blendstocks comprised primarily of aromatic species are also suitable and may be employed in the preparation of the aromatic pre-blend.

[0016] The C6-C10+ aromatic distributions and distillation profile for typical Aromatic-100 blendstocks is given in Table 1. TABLE 1TEST METHOD UNITS RESULTS SAMPLE A RESULTS SAMPLE B Distillation - IBPASTM D86°F3163255%°F32132610%°F32232620%°F32432630%°F32632740%°F32732750%°F32832760%°F32932870%°F33232880%°F33632990%°F33933095%°F340333Distillation - EP°F351345Recoveryvol %98.398.5Residuevol %1.11.0Lossvol %0.70.5GravityASTM D4052API30.530.5Density @ 60° FASTM D4052kg / m 3< 872.5872.5SulfurASTM D5453wt%<1<1Aromatics. TotalASTM D6733vol %98.399.0C8 AromaticsASTM D6733vol %5.50.2C9 AromaticsASTM D6733vol %76.692.1C10 AromaticsASTM D6733vol %15.55.9Peroxide ContentASTM D3703ppm<1<1

[0017] The compositional analysis of a typical Aromatic-150 blendstock is given in Table 2. TABLE 2ASTM D-6733Component Name WT% LV% Mol % n-Propylbenzene0.020.020.021-Methyl-3-ethylbenzene ( METOL)0.080.080.091-Methyl-4-ethylbenzene ( PETOL)0.050.050.061,3,5-Trimethylbenzene0.070.070.081-Methyl-2-ethylbenzene ( OETOL)0.070.070.081,2,4-Trimethy!benzene1.051.041.21Isobutylbenzene0.100.100.10sec-Butylbenzene0.120.120.121,2,3-Trimethylbenzene2.292.232.631 -Methy!-3-isopropylbenzene0.300.300.311-Methyl-4-isopropylbenzene1.241.261.271-Methyl-2-isopropylbenzene1.721.711.771-Methyl-3-n-propylbenzene4.584.644.711 -Methyl-4-n-propylbenzene4.644.714.771,3-Dimethyl-5-ethylbenzene5.285.305.431,2-Diethylbenzene0.450.450.461-Methyl-2-n-propylbenzene1.991.992.051,4-Dimethyl-2-ethylbenzene4.134.104.241,3-Dimethyl-4-ethylbenzene5.065.035.201,2-Dimethyl-4-ethylbenzene9.589.559.851,3-Dimethyl-2-ethylbenzene0.600.590.621,2-Dimethyl-3-Ethylbenzene2.672.612.741-ethyl-4-isopropylbenzene0.210.210.201,2,4,5-Tetramethylbenzene6.376.286.551,2,3,5-Tetramethylbenzene9.759.5510.021,2,3,4-Tetramethylbenzene1.501.451.54Pentylbenzene7.127.236.63Naphthalene1.681.481.81C11 Aromatic25.4525.6323.68Pentamethylbenzene0.020.020.022-Methylnaphthalene0.020.020.021-Methylnaphtha!ene0.010.010.01Unidentified1.782.101.71100.00100.00100.00 Table 2 Continued ASTM D-6733 Summary by Group TotalsGroup%Wt% VolParaffin0.000.00Isoparaf.0.000.00Olefin0.000.00Naphthene0.000.00Aromatic98.2297.90Oxygenates0.000.00Unidentified1.782.10100.00100.00 Summary by Carbon Totals Group %wt % Vol C40.000.00C50.000.00C60.000.00C70.000.00C80.000.00C93.633.56C1061.7661.22C1132.8333.12C120.000.00 Composition by Carbon GroupC#%wt % Vol ParaffinC40.000.00C50.000.00C60.000.00C70.000.00C80.000.00C90.000.00C100.000.00C110.000.00C120.000.00 Table 2 Continued ASTM D-6733 isoparaf.C40.000.00C50.000.00C60.000.00C70.000.00C80.000.00C90.000.00C100.000.00C110.000.00C120.000.00OlefinC40.000.00C50.000.00C60.000.00C70.000.00C80.000.00C90.000.00C100.000.00C110.000.00NaphtheneC4C50.000.00C60.000.00C70.000.00C80.000.00C90.000.00C100.000.00C110.000.00AromaticC60.000.00C70.000.00C80.000.00C93.633.56C1061.7661.22C1132.8333.12C120.000.00

[0018] The compositional analysis of another typical Aromatic-150 blendstock is given in Table 3. TABLE 3Sample ID Total Aromatic 150 WT % LV % MOL % Ortho-Xylene0.010.010.01n-Propylbenzene0.030.030.041 -Methyl-3-ethylbenzene0.100.100.121 -Methyl-4-ethylbenzene0.060.060.071,3,5-Trimethylbenzene0.110.110.131 -Methyl-2-ethylbenzene0.140.140.161,2,4-Trimethylbenzene1.261.271.48Cis 1,3 diethylcyclohexane0.010.010.01lsobutylbenzene0.060.060.06sec-Butylbenzene0.070.070.07N-Decane0.030.040.031,2,3-Trimethylbenzene1.511.491.771 -Methyl-3-isopropylbenzene0.150.150.161 -Methyl-4-isopropylbenzene0.070.070.07Indan (2,3-Dihydroindene)0.530.480.63Sec-butylcyclohexane0.010.010.011-Methyl-2-isopropylbenzene0.030.030.03Butylcyclohexane0.640.700.641-Methyl-3-n-propylbenzene2.182.232.291-Methyl-4-n-propylbenzene0.760.780.801,4-Diethylbenzene1.711.741.801,3-Dimethyl-5-ethylbenzene2.452.482.571,2-Diethylbenzene0.200.200.211-Methyl-2-n-propylbenzene1.691.701.785-Methyldecane0.030.040.032-Methyldecane0.040.050.041,4-Dimethyl-2-ethylbenzene3.093.093.251,3-Dimethyl-4-ethylbenzene0.520.520.553-Methyldecane0.020.020.021-Methylindan7.376.847.861,2-Dimethyl-4-ethylbenzene3.423.443.591,3-Dimethyl-2-ethylbenzene0.030.030.031,2-Dimethyl-3-Ethylbenzene2.662.622.79N-Undecane0.380.450.341,2,4,5-Tetramethylbenzene7.026.987.371,2,3,5-Tetramethylbenzene10.7410.6111.28 Table 3 Continued WT% LV% MOL% 4- Methylindan3.333.093.555- Methylindan3.082.863.281,2,3,4-Tetramethylbenzene5.044.915.29Pentylbenzene1.791.831.701,1 Dimethylindan0.630.590.611,2 Dimethylindan2.512.342.421,6 Dimethylindan1.341.251.29C11 Aromatic18.9819.3018.051,3,5-triethylbenzene0.270.280.231,3 Dimethylindan0.770.720.745,6 Dimethylindan0.610.570.591,2,4-triethylbenzene0.420.420.364,5 Dimethylindan0.240.220.23Tridecanes9.5810.457.72Tetradecanes1.641.761.22Pentadecanes0.120.130.08Unidentified0.520.630.55Total100,00100.00100.00Total Paraffins0.410.490.37Total Isoparaffins0.090.110.09Total Naphthenes0.660.720.66Total Aromatics86.9885.7189.31Unclassified11.8612.979.57Total C80.010.010.01Total C93.743.684.40Total C1056.3655.2659.37Total C1127.3427.3826.06Total C120.690.700.59C10 Paraffin0.030.040.03C11 Paraffin0.380.450.34C11 Isoparaffin0.090.110.09C10 Naphthene0.660.720.66C8 Aromatic0.010.010.01C9 Aromatic3.743.684.40C10 Aromatic55.6754.5058.68C11 Aromatic26.8726.8225.63C12 Aromatic0.690.700.59

[0019] The C6-C10+ aromatic distribution and distillation profile for yet another typical Aromatic-150 blendstock is given in Table 4. TABLE 4TEST METHOD UNITS RESULTS Distillation - IBPASTM D86°F3725%°F37810%°F37920%°F38030%°F38040%°F38150%°F38260%°F38370%°F38480%°F38590%°F38895%°F390Distillation - EP°F407Recoveryvol %98.8Residuevol %1.1Lossvol %0.1GravityASTM D4052API26.9Density @ 60° FASTM D4052kg / m 3< 892.5Reid Vapor PressureASTM D5191psin / aSulfurASTM D5453wt%<1Aromatics. TotalASTM D6733vol %98.8C9 AromaticsASTM D6733vol %0.7C10 AromaticsASTM D6733vol %60.5C11 AromaticsASTM D6733vol %37.6Peroxide ContentASTM D3703ppm<1Flash PointASTM D93A°F10.8

[0020] A distillation profile for a tetralin blendstock is shown in Table 5. The relatively narrow distillation range suggests that the tetralin blendstock is comprised mostly of tetralin with only relatively minor amounts of isomers and components having slightly lower or slightly higher molecular weights being present. TABLE 5TEST METHOD UNITS RESULTS Distillation - IBPASTM D86°C1995%°C202.610%°C202.720%°C202.830%°C202.940%°C20350%°C203.160%°C203.170%°C203.280%°C203.490%°C203.795%°C204.4Distillation - EP°C219.3Recoveryvol %99Residuevol %1Lossvol %0Gravity @ 15.56° CASTM D4052°API13.95

[0021] A distillation profile for a diethylbenzene blendstock is shown in Table 6. The relatively narrow distillation range suggests the diethylbenzene blendstock is comprised mostly of diethylbenzene, with only relatively minor amounts of isomers and components having slightly lower or slightly higher molecular weights being present. TABLE 6TEST METHOD UNITS RESULTS Distillation - IBPASTM D86°F353.05%°F353.210%°F353.320%°F353.530%°F353.740%°F353.950%°F354.160%°F354.370%°F354.580%°F354.790%°F355.095%°F355.6Distillation - EP°F371.6Recoveryvol %99.2Residuevol %0.8Lossvol %0.0API GravityASTM D4052°API31.6Specific GravityASTM D40520.8676

[0022] It is a relatively simple matter to determine the C6-C10+ distributions of aromatic species in the various aromatic refinery blendstocks, and determine appropriate amounts thereof that can be blended to obtain a final aromatic pre-blend having the desired C6-C10+ distribution.

[0023] The distribution of aromatic components (C6, C7, C8, C9 and C10+) for an aromatic pre-blend prepared in accordance with this disclosure, as determined analytically, is compared with the target aromatic component distribution from 40 CFR 1065.710(b) in Table 7. TABLE 7TEST METHOD UNITS Target Results MIN MAX Gravity @ 60°FASTM D4052°APIReport30.1Density @ 15.56°CASTM D4052g / mLReport0.8756Composition, aromaticsASTM D5769-C6 aromatics (benzene)vol%0.10.05-C7 aromatics (toluene)vol%23.526.024.6-C8 aromaticsvol%23.525.025.0-C9 aromaticsvol%25.027.026.3-C10+ aromaticsvol%23.026.024.8

[0024] A compositional analysis for another aromatic pre-blend prepared in accordance with this disclosure is given in Table 8. TABLE 8WT % LV % MOL % Benzene0.010.010.01Toluene23.2723.3128.44N-Octane0.010.010.01Ethylcyclohexane0.010.010.01Ethylbenzene3.143.153.33Meta-Xylene10.8510.9111.51Para-Xylene4.084.124.332-Methyloctane0.010.010.013-Methyloctane0.010.010.01Ortho-Xylene5.155.095.46N-Nonane0.010.010.01Isopropylbenzene0.050.050.05n-Propylbenzene0.140.140.131-Methyl-3-ethylbenzene0.220.220.211-Methyl-4-ethylbenzene0.230.230.221,3,5-Trimethylbenzene0.050.050.051-Methyl-2-ethylbenzene0.100.100.091,2,4-Trimethylbenzene26.4926.2924.82Isobutylbenzene0.040.040.03sec-Butylbenzene0.060.060.05N-Decane0.010.010.011,2,3-Trimethylbenzene0.050.050.051-Methyl-3-isopropylbenzene0.040.040.03Indan (2,3-Dihydroindene)0.010.010.011,3-Diethylbenzene9.369.417.851,4-Diethylbenzene12.5912.6810.561,2-Diethylbenzene0.030.030.031-Methylindan0.060.060.051,2-Dimethyl-3-Ethylbenzene0.020.020.021,2,4,5-Tetramethylbenzene0.020.020.021,2,3,5-Tetramethylbenzene0.010.010.014-Methylindan0.020.020.025-Methylindan0.010.010.01Pentylbenzene0.020.020.02Naphthalene0.310.270.27C11 Aromatic0.010.010.01N-Dodecane0.010.010.011,3,5-triethylbenzene0.020.020.015,6 Dimethylindan0.070.060.05 Table 8 Continued WT % LV % MOL % 2-Methylnaphthalene0.820.750.654,5 Dimethylindan0.050.050.04Tridecanes0.240.260.151-Methylnaphthalene0.390.330.31Tetradecanes0.190.200.11Pentadecanes0.730.770.40Hexadecanes0.410.430.21N-Hexadecane0.030.030.01Heptadecanes0.250.260.12N-Heptadecane0.010.010.00Pristane0.010.010.00Octadecanes0.040.040.02Unidentified0.230.280.16Total100.00100.00100.00Total Paraffins0.040.040.04Total Isoparaffins0.020.020.02Total Naphthenes0.010.010.01Total Aromatics97.7997.6498.75Unclassified2.142.291.18Total C60.010.010.01Total C723.2723.3128.44Total C823.2423.2924.65Total C927.3727.1725.66Total C1022.5822.6818.96Total C111.361.221.08Total C120.030.030.02C8 Paraffin0.010.010.01C9 Paraffin0.010.010.01C10 Paraffin0.010.010.01C12 Paraffin0.010.010.01C9 Isoparaffin0.020.020.02C8 Naphthene0.010.010.01C6 Aromatic0.010.010.01C7 Aromatic23.2723.3128.44C8 Aromatic23.2223.2724.63C9 Aromatic27.3427.1425.63C10 Aromatic22.5722.6718.95C11 Aromatic1.361.221.08C12 Aromatic0.020.020.01Mol WT of Sample, gm / mol112.59Density of Sample, gm / cc0.874

[0025] Total aromatics, aromatic distribution (C6, C7, C8, C9 and C10+ aromatics) and distillation profile for two additional aromatic pre-blends (DG2421BE10 and TILX353058) prepared in accordance with this disclosure are shown in Table 9. TABLE 9PRODUCT: Aromatic Pre-blend DG2421BE10TILX 353058TEST METHOD UNITS RESULTS RESULTS Distillation - IBPASTM D86°F254.0254.45%°F268.9267.910%°F271.4271.620%°F277.7277.930%°F285.0286.040%°F294.5295.450%°F305.6305.960%°F317.4317.470%°F328.6328.480%°F338.5338.690%°F351.3350.595%°F368.7368.4Distillation - EP°F437.8427.6Recoveryvol %97.897.8Residuevol %1.01.0Lossvol %1.21.2GravityASTM D4052°API30.1030.20Specific GravityASTM D4052-0.87560.8751C6 aromatics (benzene)ASTM D5769vol %0.050.05C7 aromatics (toluene)ASTM D5769vol %24.626.0C8 aromaticsASTM D5769vol %25.024.4C9 aromaticsASTM D5769vol %26.2526.45C10+ aromaticsASTM D5769vol %24.8021.40

[0026] The aromatic pre-blend can then be combined with one or more paraffinic refinery blendstocks comprised primarily of paraffinic (saturated) species and having a low aromatic content (e.g., less than 5 volume percent) to obtain a mixture meeting most of the compositional, distillation profile, and fuel quality characteristics specified in 40 CFR 1065.710(b).

[0027] The specifications for an E10 test fuel in accordance with 40 CFR 1065.710(b) is given in Table 10. TABLE 10PropertyUnitSPECIFICATIONReference ProcedureGeneral TestingLow-Temperature TestingHigh Altitude TestingAntiknock Index (R+M) / 2-87.0 - 88.487.0 MinimumASTM D2699 and D2700Sensitivity (R-M)-7.5 MinimumASTM D2699 and D2700Dry Vapor Pressure Equivalent (DVPEf'kPa (psi)60.0-63.4 (8.7-9.2)77.2-81.4 (11.2-11.8)52.4-55.2 (7.6-8.0)ASTM D5191Distillation c< 10% evaporated°C (°F)49-60 (120-140)43-54 (110-130)49-60 (120-140)ASTM D8650% evaporated°C (°F)88-99 (190-210)90% evaporated°C (°F)157-168 (315-335)Evaporated final boiling point°C (°F)193-216 (380-420)Residuemilliliter2.0 MaximumTotal Aromatic Hydrocarbonsvolume %21.0-25.0ASTM D5769C6 Aromatics (benzene)volume %0.5-0.7C7 Aromatics (toluene)volume %5.2-6.4C8 Aromaticsvolume %5.2-6.4C9 Aromaticsvolume %5.2-6.4C10+ Aromaticsvolume %4.4-5.6Olefins 5< mass %4.0-10.0ASTM D6550Ethanol blendedvolume %9.6-10.0See §1065.710(b)(3)Ethanol confirmatory f< volume %9.4-10.2ASTM D4815 or D5599Total Content of Oxygenates Other than Ethanol f< volume %0.1 MaximumASTM D4815 or D5599Sulfurmg / kg8.0-11.0ASTM D2622, D5453 or D7039Leadg / liter0.0026 MaximumASTM D3237Phosphorusg / liter0.0013 MaximumASTM D3231Copper Corrosion-No. 1 MaximumASTM D130Solvent-Washed Gum Contentmg / 100 milliliter3.0 MaximumASTM D381Oxidation Stabilityminute1000 MinimumASTM D525

[0028] To the extent that vapor pressure, olefin content, or sulfur requirements are not within the specification, butane may be added to adjust vapor pressure, olefins (such as butene) may be added to adjust olefin content, and sulfur compounds may be added to adjust sulfur content, such that the resulting composition is fully compliant with 40 CFR 1065.710(b).

[0029] Table 11 lists the test results for an E10 test fuel prepared in accordance with the methods disclosed herein. TABLE 11PRODUCT: EPA Tier 3 EEE Emission Certification Fuel, General Testing - Regular Batch No.: DE1821LT10Tank No.: 107TEST METHOD UNITS SPECIFICATIONS RESULTS MIN TARGET MAX Distillation - IBPASTM D86°F97.75%°F123.910%°F120140131.320%°F139.930%°F146.740%°F152.950%°F190210193.360%°F225.070%°F248.880%°F274.890%°F315335315.995%°F336.9Distillation - EP°F380420380.3RecoverymlReport98.0Residueml2.01.1LossmlReport1.0Gravity @ 60° FASTM D4052°APIReport58.52Density @ 15.56° CASTM D4052Report0.7440Reid Vapor Pressure EPA EquationASTM D5191psi8.79.29.1CarbonASTM D5291wt fractionReport0.8262HydrogenASTM D5291wt fractionReport0.1368Hydrogen / Carbon ratioASTM D5291mole / moleReport1.973OxygenASTM D4815wt %Report3.70Ethanol contentASTM D5599-00vol %9.610.09.9Total oxygentates other than ethanolASTM D4815vol %0.1None DetectedSulfurASTM D5453mg / kg8.011.010.1PhosphorusASTM D3231g / l0.0013None DetectedLeadASTM D3237g / l0.0026None DetectedComposition, aromaticsASTM D5769vol %21.025.023.3C6 aromatics (benzene)ASTM D5769vol %0.50.70.6C7 aromatics (toluene)ASTM D5769vol %5.26.45.9C8 aromaticsASTM D5769vol %5.26.46.1C9 aromaticsASTM D5769vol %5.26.45.6C10+ aromaticsASTM D5769vol %4.45.65.1Composition, olefinsASTM D6550wt %4.010.05.8Oxidation StabilityASTM D525minutes10001000+Copper CorrosionASTM D13011aExistent gum, washedASTM D381mg / 100mls3.01.0Existent gum, unwashedASTM D381mg / 100mlsReport1.5Research Octane NumberASTM D2699Report92.1Motor Octane NumberASTM D2700Report83.7R+M / 2D2699 / 270087.088.487.9SensitivityD2699 / 27007.58.4Net Heat of CombustionASTM D240BTU / lbReport17954

[0030] The described embodiments are not limiting. Various modifications are considered within the purview and scope of the appended claims.

Claims

1. A process for preparing E10 test fuel in accordance with 40 CFR 1065.710(b), comprising: (a) providing an aromatic pre-blend prepared by mixing aromatic refinery blendstocks comprising at least one of Aromatic-100, Aromatic-150, Aromatic-200, combined with at least one of benzene, toluene, xylene, 1,2,4-trimethyl benzene, 1,3,5-trimethyl benzene, diethylbenzene, and tetralin in proportions that produce a mixture comprising aromatic compounds in proportions as specified in 40 CFR 1065.710(b) (as published April 28, 2014 at 79 FR 23809); (b) combining the aromatic pre-blend with at least one paraffinic refinery blendstock having a paraffin (saturates) content of at least 93 volume percent, an aromatic content less than 10 volume percent, an initial boiling point of at least 82°F (28°C), and a final boiling point from 380°F (193°C) to 435°F (224°C), the aromatic pre-blend, and refinery blendstock being mixed with ethanol in proportions effective to achieve the specified aromatic distribution, total aromatics content, ethanol content and distillation profile of 40 CFR 1065.710(b); and (c) adding butane, olefin-containing blendstocks, and sulfur compounds or sulfur-containing blendstocks as needed to meet the requirements of 40 CFR 1065.710(b).

2. The process of Claim 1, in which the aromatic pre-blend is formulated to have a total aromatic compound content of at least 90 volume percent.

3. The process of Claim 1, in which the at least one paraffinic refinery blendstock comprises 5 volume percent or less aromatic compounds.

4. An aromatic pre-blend for use in preparing E10 test fuel in accordance with 40 CFR 1065.710(b), the aromatic pre-blend comprising: a mixture of aromatic refinery blendstocks including (i) at least one of Aromatic-100, Aromatic-150 and Aromatic-200; and (ii) at least one of benzene, toluene, xylene, trimethyl benzene, diethyl benzene and tetralin, the resulting mixture having a C7:C6 ratio in units of volume of 5.2-6.4:0.5-0.7, a C8:C6 ratio in units of volume of 5.2-6.4:0.5-0.7, a C9:C6 ratio in units of volume of 5.2-6.4:0.5-0.7, and a C10+:C6 ratio in units of volume of 4.4-5.6:0.5-0.7, and a total aromatic compound content of at least 90 volume percent.

5. The aromatic pre-blend of claim 4, having a total aromatic compound content of at least 95 volume percent.

6. The aromatic pre-blend of claim 4, having a total aromatic compound content of at least 98 volume percent.