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Designation: D 7467 – 09a Standard Specification for Diesel Fuel Oil, Biodiesel Blend (B6 to B20) 1 This standard is issued under the fixed designation D 7467; the number immediately following the designation indicates the year of original adoption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval. A superscript epsilon (´) indicates an editorial change since the last revision or reapproval. 1. Scope* 1.1 This specification covers fuel blend grades of 6 to 20 volume percent (%) biodiesel with the remainder being a light middle or middle distillate diesel fuel, collectively designated as B6 to B20. These grades are suitable for various types of diesel engines. 1.1.1 The biodiesel component of the blend shall conform to the requirements of Specification D 6751. The remainder of the fuel shall be a light middle or middle distillate grade diesel fuel conforming to Specification D 975 grades No. 1-D and No. 2-D of any sulfur level specified with the following exceptions. The light middle or middle distillate grade diesel fuel whose sulfur level, aromatic level, cetane, or lubricity falls outside of Specification D 975 may be blended with biodiesel meeting Specification D 6751, provided the finished mixtures meets this specification. 1.1.2 The fuel sulfur grades are described as follows: 1.1.2.1 Grade B6 to B20 S15—A fuel with a maximum of 15 ppm sulfur. 1.1.2.2 Grade B6 to B20 S500—A fuel with a maximum of 500 ppm sulfur. 1.1.2.3 Grade B6 to B20 S5000—A fuel with a maximum of 5000 ppm sulfur. 1.2 This specification prescribes the required properties of B6 to B20 biodiesel blends at the time and place of delivery. The specification requirements may be applied at other points in the production and distribution system when provided by agreement between the purchaser and the supplier. 1.2.1 Nothing in this specification shall preclude observance of federal, state, or local regulations that may be more restrictive. NOTE 1—The generation and dissipation of static electricity can create problems in the handling of distillate diesel fuel oils. For more informa- tion on this subject, see Guide D 4865. 1.3 The values stated in SI units are to be regarded as standard. No other units of measurement are included in this standard. 2. Referenced Documents 2.1 ASTM Standards: 2 D 56 Test Method for Flash Point by Tag Closed Cup Tester D 86 Test Method for Distillation of Petroleum Products at Atmospheric Pressure D 93 Test Methods for Flash Point by Pensky-Martens Closed Cup Tester D 129 Test Method for Sulfur in Petroleum Products (Gen- eral Bomb Method) D 130 Test Method for Corrosiveness to Copper from Petroleum Products by Copper Strip Test D 445 Test Method for Kinematic Viscosity of Transparent and Opaque Liquids (and Calculation of Dynamic Viscos- ity) D 482 Test Method for Ash from Petroleum Products D 524 Test Method for Ramsbottom Carbon Residue of Petroleum Products D 613 Test Method for Cetane Number of Diesel Fuel Oil D 664 Test Method for Acid Number of Petroleum Products by Potentiometric Titration D 975 Specification for Diesel Fuel Oils D 976 Test Method for Calculated Cetane Index of Distil- late Fuels D 1266 Test Method for Sulfur in Petroleum Products (Lamp Method) D 1319 Test Method for Hydrocarbon Types in Liquid Petroleum Products by Fluorescent Indicator Adsorption D 1552 Test Method for Sulfur in Petroleum Products (High-Temperature Method) D 2500 Test Method for Cloud Point of Petroleum Products D 2622 Test Method for Sulfur in Petroleum Products by Wavelength Dispersive X-ray Fluorescence Spectrometry D 2709 Test Method for Water and Sediment in Middle Distillate Fuels by Centrifuge D 2880 Specification for Gas Turbine Fuel Oils D 3117 Test Method for Wax Appearance Point of Distillate Fuels D 3120 Test Method for Trace Quantities of Sulfur in Light 1 This specification is under the jurisdiction of ASTM Committee D02 on Petroleum Products and Lubricants and is the direct responsibility of Subcommittee D02.E0 on Burner, Diesel, Non-Aviation Gas Turbine, and Marine Fuels. Current edition approved April 15, 2009. Published June 2009. Originally approved in 2008. Last previous edition approved in 2009 as D 7467 – 09. 2 For referenced ASTM standards, visit the ASTM website, www.astm.org, or contact ASTM Customer Service at [email protected]. For Annual Book of ASTM Standards volume information, refer to the standard’s Document Summary page on the ASTM website. 1 *A Summary of Changes section appears at the end of this standard. Copyright (C) ASTM International, 100 Barr Harbour Dr. P.O. box C-700 West Conshohocken, Pennsylvania 19428-2959, United States Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009 Downloaded/printed by Stephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.

ASTM D 7467, Standard Specification for Diesel Fuel Oil, Biodiesel Blend (B6 to B20), 2009

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Designation: D 7467 09aStandard Specication forDiesel Fuel Oil, Biodiesel Blend (B6 to B20)1ThisstandardisissuedunderthexeddesignationD 7467;thenumberimmediatelyfollowingthedesignationindicatestheyearoforiginal adoption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval. Asuperscript epsilon () indicates an editorial change since the last revision or reapproval.1. Scope*1.1Thisspecicationcoversfuel blendgradesof6to20volume percent (%) biodiesel with the remainder being a lightmiddle or middle distillate diesel fuel, collectively designatedasB6toB20.Thesegradesaresuitableforvarioustypesofdiesel engines.1.1.1The biodiesel component of the blend shall conform tothe requirements of Specication D 6751. The remainder of thefuel shall be a light middle or middle distillate grade diesel fuelconformingtoSpecicationD 975gradesNo. 1-DandNo.2-D of any sulfur level specied with the following exceptions.Thelightmiddleormiddledistillategradedieselfuelwhosesulfur level, aromatic level, cetane, or lubricity falls outside ofSpecicationD 975maybeblendedwithbiodiesel meetingSpecication D 6751, provided the nished mixtures meets thisspecication.1.1.2The fuel sulfur grades are described as follows:1.1.2.1GradeB6toB20S15A fuel with a maximum of15 ppm sulfur.1.1.2.2Grade B6 to B20 S500A fuel with a maximum of500 ppm sulfur.1.1.2.3Grade B6 to B20 S5000Afuel with a maximum of5000 ppm sulfur.1.2ThisspecicationprescribestherequiredpropertiesofB6 to B20 biodiesel blends at the time and place of delivery.The specication requirements may be applied at other pointsintheproductionanddistributionsystemwhenprovidedbyagreement between the purchaser and the supplier.1.2.1Nothing in this specication shall preclude observanceof federal, state, or local regulations that may be morerestrictive.NOTE 1The generation and dissipation of static electricity can createproblems in the handling of distillate diesel fuel oils. For more informa-tion on this subject, see Guide D 4865.1.3The values statedinSI units are tobe regardedasstandard.Nootherunitsofmeasurementareincludedinthisstandard.2. Referenced Documents2.1ASTM Standards:2D 56Test Method for Flash Point by Tag Closed Cup TesterD 86Test Method for Distillation of Petroleum Products atAtmospheric PressureD 93Test Methods for Flash Point by Pensky-MartensClosed Cup TesterD 129Test Method for Sulfur in Petroleum Products (Gen-eral Bomb Method)D 130Test Method for Corrosiveness to Copper fromPetroleum Products by Copper Strip TestD 445Test Method for Kinematic Viscosity of Transparentand Opaque Liquids (and Calculation of Dynamic Viscos-ity)D 482Test Method for Ash from Petroleum ProductsD 524Test Method for RamsbottomCarbon Residue ofPetroleum ProductsD 613Test Method for Cetane Number of Diesel Fuel OilD 664Test Method for Acid Number of Petroleum Productsby Potentiometric TitrationD 975Specication for Diesel Fuel OilsD 976TestMethodforCalculatedCetaneIndexofDistil-late FuelsD 1266Test Method for Sulfur in PetroleumProducts(Lamp Method)D 1319Test Method for Hydrocarbon Types in LiquidPetroleum Products by Fluorescent Indicator AdsorptionD 1552Test Method for Sulfur in PetroleumProducts(High-Temperature Method)D 2500Test Method for Cloud Point of Petroleum ProductsD 2622Test MethodforSulfurinPetroleumProductsbyWavelength Dispersive X-ray Fluorescence SpectrometryD 2709Test Methodfor Water andSediment inMiddleDistillate Fuels by CentrifugeD 2880Specication for Gas Turbine Fuel OilsD 3117Test Method for Wax Appearance Point of DistillateFuelsD 3120Test Method for Trace Quantities of Sulfur in Light1This specication is under the jurisdiction of ASTMCommittee D02 onPetroleum Products and Lubricants and is the direct responsibility of SubcommitteeD02.E0 on Burner, Diesel, Non-Aviation Gas Turbine, and Marine Fuels.Current edition approvedApril 15, 2009. Published June 2009. Originallyapproved in 2008. Last previous edition approved in 2009 as D 7467 09.2Forreferenced ASTMstandards, visit the ASTMwebsite, www.astm.org, orcontact ASTM Customer Service at [email protected]. For Annual Book of ASTMStandards volume information, refer to the standards Document Summary page onthe ASTM website.1*A Summary of Changes section appears at the end of this standard.Copyright (C) ASTM International, 100 Barr Harbour Dr. P.O. box C-700 West Conshohocken, Pennsylvania 19428-2959, United StatesCopyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.LiquidPetroleumHydrocarbonsbyOxidativeMicrocou-lometryD 3828Test Methods for Flash Point by Small Scale ClosedCup TesterD 4057Practice for Manual Samplingof PetroleumandPetroleum ProductsD 4294Test Method for Sulfur in Petroleum and PetroleumProducts by Energy Dispersive X-ray Fluorescence Spec-trometryD 4539Test Methodfor Filterabilityof Diesel Fuels byLow-Temperature Flow Test (LTFT)D 4737TestMethodforCalculatedCetaneIndexbyFourVariable EquationD 4865Guide for Generation and Dissipation of StaticElectricity in Petroleum Fuel SystemsD 5453Test MethodforDeterminationofTotal SulfurinLight Hydrocarbons, SparkIgnitionEngineFuel, DieselEngine Fuel, and Engine Oil by Ultraviolet FluorescenceD 5771Test Method for Cloud Point of Petroleum Products(Optical Detection Stepped Cooling Method)D 5772Test Method for Cloud Point of Petroleum Products(Linear Cooling Rate Method)D 5773Test Method for Cloud Point of Petroleum Products(Constant Cooling Rate Method)D 6079Test Method for Evaluating Lubricity of DieselFuels by the High-Frequency Reciprocating Rig (HFRR)D 6217 Test Method for Particulate Contamination inMiddle Distillate Fuels by Laboratory FiltrationD 6371Test Method for Cold Filter Plugging Point ofDiesel and Heating FuelsD 6468Test Method for High Temperature Stability ofMiddle Distillate FuelsD 6469Guidefor Microbial ContaminationinFuels andFuel SystemsD 6751 Specication for Biodiesel Fuel Blend Stock(B100) for Middle Distillate FuelsD 6890Test Methodfor Determinationof IgnitionDelayand Derived Cetane Number (DCN) of Diesel Fuel Oils byCombustion in a Constant Volume ChamberD 7371Test Method for Determination of Biodiesel (FattyAcid Methyl Esters) Content in Diesel Fuel Oil Using MidInfrared Spectroscopy (FTIR-ATR-PLS Method)D 7397Test Method for Cloud Point of Petroleum Products(Miniaturized Optical Method)E 29PracticeforUsingSignicant DigitsinTest DatatoDetermine Conformance with Specications2.2 Other Standards:26 CFR Part 48Manufacturers and Retailers Excise Taxes340 CFR Part 80Regulation of Fuels and Fuel Additives3EN14078Liquidpetroleumproducts - Determinationoffattyacidmethylester(FAME)contentinmiddledistil-lates - Infrared spectrometry method4EN 14112 Fat and oil derivatives - Fatty acid methyl esters(FAME)-Determinationofoxidationstability(Acceler-ated oxidation test)43. Terminology3.1Denitions:3.2biodiesel, nfuel comprisedof mono-alkyl esters oflongchainfattyacidsderivedfromvegetableoilsoranimalfats, designated B100.3.3B6 to B20, nfuel blend consisting of 6 to 20 volumepercent biodiesel conformingtotherequirementsofSpeci-cationD 6751withthe remainder beinga light middle ormiddle distillate grade diesel fuel and meeting the requirementsof this specication.3.3.1DiscussionThe abbreviation BXX represents a spe-cic blend concentration in the range B6 to B20, where XX isthe percent volume of biodiesel in the fuel blend.3.4 S(numerical specication maximum)indicates themaximum sulfur content, in weight ppm (g/g), allowed by thisspecication.4. Test Methods4.1The requirements enumerated in this specication shallbe determined in accordance with the following methods:4.1.1Acid NumberTest Method D 664.4.1.2FlashPointTestMethodD 93, exceptwhereothermethodsareprescribedbylaw.TestMethodD 3828maybeusedasanalternatewiththesamelimits.Test MethodD 56may be used as an alternate with the same limits, provided theash point is below 93C. This test method will give slightlylowervalues.Incasesofdispute, TestMethodD 93shallbeused as the referee method.4.1.3Cloud PointTest Method D 2500. For all B6 to B20grades in Table 1, Test Method D 7397 and the automatic TestMethods D 5771, D 5772, or D 5773 may be used as alternateswiththesamelimits.TestMethodD 3117mayalsobeusedsinceit iscloselyrelatedtoTest MethodD 2500. Incaseofdispute, Test Method D 2500 shall be the referee test method.4.1.4Cold Filter Plugging Point (CFPP)Test MethodD 6371.4.1.5LowTemperature FlowTest (LTFT)Test MethodD 4539.4.1.6Water and SedimentTest Method D 2709.4.1.7Carbon ResidueTest Method D 524.4.1.8AshTest Method D 482.4.1.9DistillationTest Method D 86.4.1.10ViscosityTest Method D 445.4.1.11SulfurTable 2 shows the referee test methods andalternate test methods for sulfur, the range over which each testmethod applies and the corresponding fuel grades.4.1.12AromaticityTest Method D 1319. This test methodprovidesanindicationof thearomaticcontent of fuels. Forfuelswithamaximumnalboilingpointof315C, thistestmethod is a measurement of the aromatic content of the fuel.Grade S5000 does not have an aromatics content.4.1.13Cetane IndexTest Method D 976.4.1.14LubricityTest Method D 6079.4.1.15CopperCorrosionTestMethodD 130, 3htestat50C minimum.3Available from U.S. Government Printing Office Superintendent of Documents,732 N. Capitol St., NW, Mail Stop: SDE, Washington, DC 20401.4Available fromthe National CENmembers listed on the CENwebsite(www.cenorm.be.) or from the CEN/TC 19 Secretariat ([email protected]).D 7467 09a2Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.4.1.16CetaneNumberTest MethodD 613. Test MethodD 6890mayalsobeused. Incasesof dispute, Test MethodD 613 shall be the referee test method.4.1.17Oxidation StabilityTest Method EN 14112. Thesubcommittee is aware of potential issues in the current versionwhen used for biodiesel blends. This standard is being revisedto resolve these issues. See X1.16.2 for further information.TABLE 1 Detailed Requirements for B6 to B20 Biodiesel BlendsProperty Test MethodGradeB6 to B20 S15 B6 to B20 S500AB6 to B20 S5000BAcid Number, mg KOH/g, max D 664 0.3 0.3 0.3Viscosity, mm2/s at 40C D 445 1.9-4.1C1.9-4.1C1.9- 4.1CFlash Point, C, min D 93 52D52D52DCloud Point, C, max or LTFT/CFPP, C, max D 2500, D 4539, D 6371E E ESulfur Content, (g/g) D 5453 15 ... ...mass %, max D 2622 ... 0.05 ...mass %, max D 129 ... ... 0.50Distillation Temperature, C, 90% vol recovered, max D 86 343 343 343Ramsbottom Carbon Residue on 10% bottoms, mass %, max D 524 0.35 0.35 0.35Cetane Number, min D 613F40G40G40GOne of the following must be met:(1) Cetane index, min.D 976-80H40 40 40(2) Aromaticity, %vol, max D 1319-03H35 35 ...Ash Content, mass%, max D 482 0.01 0.01 0.01Water and Sediment, volume%, max D 2709 0.05 0.05 0.05Copper Corrosion, 3 h at 50C, max D 130 No. 3 No. 3 No. 3Biodiesel Content, % (V/V) D 7371 6. - 20. 6. - 20. 6. - 20.Oxidation Stability, hours, min EN 14112 6 6 6Lubricity, HFRR at 60C, micron (m), max D 6079 520I520I520IAUnder United States of America regulations, if Grades B6-20 S500 are sold for tax exempt purposes then, at, or beyond terminal storage tanks, they are required by26 CFR Part 48 to contain the dye Solvent Red 164 at a concentration spectrally equivalent to 3.9 lb per thousand barrels of the solid dye standard Solvent Red 164, orthe tax must be collected.BUnder United States of America regulations, Grades B6-20 S5000 are required by 40 CFR part 80 to contain a sufficient amount of the dye Solvent Red 164 so itspresence is visually apparent. At or beyond terminal storage tanks, they are required by 26 CFR Part 48 to contain the dye Solvent Red 164 at a concentration spectrallyequivalent to 3.9 lb per thousand barrels of the solid dye standard Solvent Red 26.CIf Grade No. 1-D or blends of Grade No. 1-D and Grade No. 2-D diesel fuel are used, the minimum viscosity shall be 1.3 mm2/s.DIf Grade No. 1-D or blends of Grade No. 1-D and Grade No. 2-D diesel fuel are used, or a cloud point of less than -12C is specied, the minimum ash point shallbe 38C.EIt is unrealistic to specify low temperature properties that will ensure satisfactory operation at all ambient conditions. In general, cloud point (or wax appearance point)Low Temperature Flow Test, and Cold Filter Plugging Point Test may be useful to estimate vehicle low temperature operability limits but their use with B6 to B20 has notbeen validated. However, satisfactory operation below the cloud point (or wax appearance point) may be achieved depending on equipment design, operating conditions,and the use of ow-improver additives as described in X3.1.2. Appropriate low temperature operability properties should be agreed upon between the fuel supplier andpurchaserfortheintendeduseandexpectedambienttemperatures. TestMethodsD 4539andD 6371maybeespeciallyuseful toestimatevehiclelowtemperatureoperability limits when ow improvers are used but their use with B6 to B20 from a full range of biodiesel feedstock sources has not been validated. Due to fuel deliverysystem, engine design, and test method differences, low temperature operability tests may not provide the same degree of protection in various vehicle operating classes.Tenth percentile minimum air temperatures for U.S. locations are provided in Appendix X3 as a means of estimating expected regional temperatures. The tenth percentileminimum air temperatures may be used to estimate expected regional target temperatures for use with Test Methods D 2500, D 4539, and D 6371. Refer to X3.1.3 forfurther general guidance on test application.FCalculated cetane index approximation, Test Method D 4737, is not applicable to biodiesel blends.GLow ambient temperatures, as well as engine operation at high altitudes, may require the use of fuels with higher cetane ratings. If the diesel fuel is qualied underTable 1ofSpecicationD 975forcetane,itisnotnecessarytomeasurethecetanenumberoftheblend. Thisisbecausethecetanenumberoftheindividual blendcomponents will be at least 40, so the resulting blend will also be at least 40 cetane number.HThese test methods are specied in 40 CFR Part 80.IIf the diesel fuel is qualied under Table 1 of Specication D 975 for lubricity, it is not necessary to measure the lubricity of the blend. This is because the lubricity ofthe individual blend components will be less than 520 micron (m) so the resulting blend will also be less than 520 (m).TABLE 2Sulfur Test MethodsSulfur Test Method Range Grades Units Used to Report ResultsAD 129(referee)>0.1 mass % S5000 mass %D 1266 0.0005 to 0.4 mass %5 to 4000 mg/kg (wt ppm)S500 mass %D 1552 >0.06 mass % S5000 mass %D 2622(referee for S500 grades)0.0003 to 5.3 mass %3 to 53 000 mg/kg (wt ppm)all grades mass %D 3120 3.0 to 100 mg/kg (wt ppm) S15, S500(S500 grades must be diluted before testing)ppm (g/g)D 4294 0.0150 to 5.00 mass %150 to 50 000 mg/kg (wt ppm)S5000 mass %D 5453(referee for S15 grades)0.0001 to 0.8 mass %1.0 to 8000 mg/kg (wt ppm)all grades ppm (g/g)AResults reported in mg/kg and in ppm (g/g) are numerically the same. The units used in Table 1 for the sulfur requirements are the units in which results for the refereetest are reported.D 7467 09a3Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.4.1.18 Biodiesel ContentTest Method D 7371. TestMethod EN 14078 may also be used. In cases of dispute, TestMethod D 7371 shall be the referee test method. See PracticeE 29 for guidance on signicant digits.5. Workmanship5.1The biodiesel blend (B6 to B20) shall be visually free ofundissolved water, sediment, and suspended matter.5.2The biodiesel blend (B6 to B20) shall also be free of anyadulterantorcontaminantthatmayrenderthefuelunaccept-able for its commonly used applications.6. Requirements6.1The biodiesel blend (B6 to B20) specied shall conformto the detailed requirements shown in Table 1.7. Keywords7.1biodiesel; biodiesel blend; diesel; fuel oil; petroleumand petroleum productsAPPENDIXES(Nonmandatory Information)X1. SIGNIFICANCE OF ASTM SPECIFICATION FOR B6 to B20 BIODIESEL BLENDSX1.1IntroductionX1.1.1 Theproperties of commercial B6toB20blendsdepend on the rening practices employed and the nature of thedistillate fuel oils and biodiesel from which they are produced.Distillatefueloils, forexample, maybeproducedwithintheboiling range of 150 and 400C having many possible combi-nations of various properties, such as volatility, ignition qual-ity, viscosity, and other characteristics. Biodiesel, for example,can be produced from a variety of animal fats or vegetable oilsthatproducesimilarvolatilitycharacteristicsandcombustionemissions with varying cold ow properties.X1.2Cetane NumberX1.2.1Cetane number is a measure of the ignition quality ofthe fuel and inuences combustion roughness. The cetanenumber requirements depend on engine design, size, nature ofspeedandloadvariations, andonstartingandatmosphericconditions. Increase incetane number over values actuallyrequired does not materially improve engine performance.Accordingly, the cetane number specied should be as low aspossible to ensure maximum fuel availability.X1.3DistillationX1.3.1Thefuel volatilityrequirementsdependonenginedesign, size, nature of speed and load variations, and startingand atmospheric conditions. For engines in services involvingrapidly uctuating loads and speeds, as in bus and truckoperation, themorevolatilefuels mayprovidebest perfor-mance, particularly with respect to smoke and odor. Thebiodiesel portion of the B6 to B20 may also provide smoke andodor improvements. However, best fuel economy is generallyobtained from the heavier types of fuels because of their higherheat content.X1.4ViscosityX1.4.1For someengines it is advantageous tospecifyaminimumviscositybecause of power loss due toinjectionpumpandinjectorleakage.Maximumviscosity,ontheotherhand, islimitedbyconsiderationsinvolvedinenginedesignand size, and the characteristics of the injection system.X1.5Carbon ResidueX1.5.1Carbon residue gives a measure of the carbondepositing tendencies of a fuel oil when heated in a bulb underprescribed conditions. While not directly correlating withengine deposits, this property is considered an approximation.X1.6SulfurX1.6.1The effect of sulfur content onengine wear anddeposits appears to vary considerably in importance anddepends largely on operating conditions. Fuel sulfur can affectemissioncontrol systemsperformance. Toensuremaximumavailabilityoffuels, thepermissiblesulfurcontentshouldbespecied as high as is practicable, consistent with maintenanceconsiderations and legal limits.X1.7Flash PointX1.7.1The ash point as specied is not directly related toengine performance. It is, however, of importance in connec-tion with legal requirements and safety precautions involved infuel handling and storage, and it is normally specied to meetinsurance and re regulations.X1.8Cloud PointX1.8.1Cloudpoint isofimportanceinthat it denesthetemperature at which a cloud or haze of wax crystals appearsin the oil under prescribed test conditions that generally relatestothetemperatureatwhichwaxcrystalsbegintoprecipitatefrom the oil in use.X1.9AshX1.9.1Ash-forming materials may be present in fuel oil inthree forms: (1) abrasive solids, (2) soluble metallic soaps, and(3)unremovedbiodiesel catalysts. Abrasivesolidsandunre-movedbiodiesel catalysts contributetoinjector, fuel pump,pistonandringwear, andalsotoengine deposits. Solublemetallic soaps have little effect on wear but may contribute toengine deposits and lter clogging.D 7467 09a4Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.X1.10Copper Strip CorrosionX1.10.1This test serves as a measure of possible difficultieswith copper and brass or bronze parts of the fuel system.X1.11AromaticityX1.11.1Thistestisusedasanindicationofthearomaticscontent of diesel fuel. Aromatics content is specied to preventanincreaseintheaveragearomaticscontent indiesel fuels.Increases in aromatics content of fuels over current levels mayhave a negative impact onemissions. Use of Test MethodD 1319-03 or cetane index, Test Method D 976-80, is requiredinthe UnitedStates of America by40CFRPart 80. TheprecisionandbiasofTest MethodD 1319-03withbiodieselblends is not known and is currently under investigation.X1.12Cetane IndexX1.12.1Cetane indexis speciedas a limitationontheamount of high aromatic components in S15 and S500 Grades.Useof TestMethodD 1319-03orcetaneindex, TestMethodD 976-80, isrequiredintheUnitedStatesof Americaby40CFR Part 80. The precision and bias of Test Method D 976-80with biodiesel blends is not known.X1.13Total and Free GlycerinX1.13.1High levels of total or free glycerin can causeinjector deposits and may adversely affect cold weather opera-tion and lter plugging and result in a buildup of material in thebottomof storage andfuelingsystems. The total andfreeglycerin levels are controlled by Specication D 6751 to 0.24%mass maximumand 0.02%mass maximum, respectively.Dieselfuelcontainsnototalorfreeglycerin, sotheleveloftotal andfreeglycerininabiodiesel blendissolelyderivedfromthebiodiesel contributionandisextremelylowandindirectproportiontothelevelofbiodieseladdedanditstotaland free glycerin values. In nished blends, the ability tomeasure total and free glycerin is compromised by interferencewith naturally occurring petroleum diesel fuel components andthe extremely low values. No ASTM test methods for measur-ingtotal andfree glycerininblends currentlyexist, sonospecicationforthenishedB6toB20blendisincluded. Iftest methods become available, the level of total and freeglycerin should not exceed the maximum contribution derivedfrombiodieselbasedontheblendcontentandthemaximumlevel allowed in Specication D 6751.X1.14Calcium and Magnesium, Sodium and Potassium,and Phosphorus ContentX1.14.1Calciumand magnesiumcombined and sodiumand potassium combined are controlled to 5 ppm maximum inSpecication D 6751. Phosphorus is controlled to 10 ppmmaximum in Specication D 6751. The presence of high levelsof these elements could adversely affect exhaust catalysts andafter-treatment systems. Theconcentrationofthesematerialsdue to biodiesel in a B6 to B20 blends should be less than 1 or2 ppm, making accurate measurement difficult. There are alsono controls for these materials in Specication D 975 at presentand no available database for the potential contribution of thesematerialsfrompetroleumbaseddiesel fuel. Basedonthis, aspecication for nished blends for these compounds has notbeen established. If measured, the level of these materialsshouldnot exceedthemaximumcontributionderivedfrombiodieselbasedontheblendcontentandthemaximumlevelallowedinSpecicationD 6751andthecontributionof thepetroleum based diesel fuel.X1.15OtherX1.15.1Microbial Contamination:X1.15.1.1Uncontrolled microbial contamination in fuelsystems can cause or contribute to a variety of problems,includingincreasedcorrosivityanddecreasedstability, lter-ability, and caloric value. Microbial processes in fuel systemscan also cause or contribute to system damage.X1.15.1.2Becausethemicrobescontributingtotheafore-mentionedproblems arenot necessarilypresent inthefuelitself, no microbial quality criterion for fuels is recommended.However, it isimportant that personnel responsiblefor fuelquality understand how uncontrolled microbial contaminationcan affect fuel quality.X1.15.1.3GuideD 6469provides personnel withlimitedmicrobiological backgroundanunderstandingof the symp-toms, occurrences, and consequences of microbial contamina-tion. Guide D 6469 also suggests means for detecting andcontrolling microbial contamination in fuels and fuel systems.Good housekeeping, especially keeping fuel dry, is critical.X1.16Oxidation StabilityX1.16.1If the biodiesel is qualied under Table 1 of Speci-cation D 6751 for oxidation stability, it may not be necessaryto measure the oxidation stability of the blend. Existing data5indicates the oxidation stability of B6 to B20 should be over 6h if the oxidation stability of the biodiesel is 3 h or higher at thetime of blending.X1.16.2Special precautions may be necessary to eliminatefalselylowreadings usingEN 14112withbiodiesel blends.The petroleum portion of the blend may affect tubing betweenthe reaction vessel and the measuring vessel and the plastic sealon the top of the reaction vessel or condense in various parts ofthetest setup. Someofthesepartsmayneedtobereplacedfrequently, and all components should be thoroughly cleaned toprevent falsely low readings. Improvements to these parts andpotential changes in the test method are currently beingevaluated.X1.17Acid NumberX1.17.1The acid number is used to determine the level offree fatty acids or processing acids that may be present in thebiodiesel or diesel fuel oil when produced, or those which formuponaging. Biodiesel blendswithahighacidnumberhavebeen shown to increase fueling systemdeposits and mayincrease the likelihood for corrosion.5McCormick, R. L., and Westbrook, S. R., Empirical Study of the Stability ofBiodiesel and Biodiesel Blends, Milestone Report, NREL/TP-540-41619, NationalRenewable Energy Laboratory, Golden, Colorado, May 2007. http://www.nrel.gov/docs/fy07osti/41619.pdf.D 7467 09a5Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.X2. STORAGE AND THERMAL STABILITY OF B6 TO B20 BLENDSX2.1ScopeX2.1.1ThisappendixprovidesguidanceforconsumersofB6 to B20 who may wish to store quantities of fuels forextendedperiods or use the fuel insevere service or hightemperature applications. Fuels containing residual compo-nents are excluded. Consistently successful long-termfuelstorage or use in severe applications requires attention to fuelselection, storage conditions, handling and monitoring ofproperties during storage and prior to use.X2.1.2Normally produced fuels have adequate stabilityproperties towithstandnormal storageandusewithout theformationof troublesomeamounts of insolubledegradationproductsalthoughdatasuggestssomeB6toB20blendsmaydegrade faster than petrodiesel. Fuels that are to be stored forprolongedperiods or usedinsevereapplications shouldbeselectedtoavoidformationofsedimentsorgums, highacidnumbers, or high viscosity which can overload lters or pluginjectors. Selection of these fuels should result from supplier-user discussions.X2.1.3These suggested practices are general in nature andshould not be considered substitutes for any requirementsimposed by the warranty of the distillate fuel equipmentmanufacturer or by federal, state, or local government regula-tions. Although they cannot replace a knowledge of localconditions or good engineering and scientic judgment, thesesuggested practices do provide guidance in developing anindividual fuel management system for the B6 to B20 fuel user.They include suggestions in the operation and maintenance ofexisting fuel storage and handling facilities and for identifyingwhere, when, andhowfuel qualityshouldbemonitoredorselected for storage or severe use.X2.2DenitionsX2.2.1bulkfuelfuel inthestoragefacilityinquantitiesover 50 gal.X2.2.2fuel contaminantsforeign materials that make fuelless suitable or unsuitable for the intended use.X2.2.2.1DiscussionFuelcontaminantsincludematerialsintroducedsubsequentto the manufacture of fuel and fuel degradation products.X2.2.3fuel-degradation productsthose materials that areformedinfuel duringextendedstorageor exposuretohightemperatures.X2.2.3.1DiscussionInsolubledegradationproductsmaycombine with other fuel contaminants to reinforce deleteriouseffects. Solubledegradationproducts(solublegums)arelessvolatilethanfuelandmaycarbonizetoformdepositsduetocomplex interactions and oxidation of small amounts ofolenicor sulfur-, oxygen-, or nitrogen-contaminatingcom-pounds present in fuels. The formation of degradation productsmay be catalyzed by dissolved metals, especially copper salts.Whendissolvedcopperispresent it canbedeactivatedwithmetal deactivator additives.X2.2.4long-term storagestorage of fuel for longer than 6months after it is received by the user.X2.2.5severeuseuseof thefuel inapplications whichmay result in engines operating under high load conditions thatmay cause the fuel to be exposed to excessive heat.X2.3Fuel SelectionX2.3.1Certain distilled renery and biodiesel products aregenerally more suitable for long-termstorage and severeservice than others. The stability properties of B6 to B20blends are highly dependent on the crude oil sources, severityof processing, use of additives and whether additional renerytreatment has been carried out.X2.3.2 ThecompositionandstabilitypropertiesofB6toB20 produced at specic reneries or blending locations maybe different. Anyspecial requirements of the user, suchaslong-term storage or severe service, should be discussed withthe supplier.X2.3.3 Blends of fuels from various sources may interact togive stabilityproperties worse thanexpectedbasedonthecharacteristics of the individual fuels.X2.4Fuel AdditivesX2.4.1Availablefueladditivescanimprovethesuitabilityofmarginalfuelsforlong-termstorageandthermalstability,but may be unsuccessful for fuels with markedly poor stabilityproperties. Mostadditivesshouldbeaddedatthereneryorduring the early weeks of storage to obtain maximum benets.X2.4.2Biocides or biostats destroy or inhibit the growth offungi and bacteria, which can grow at fuel-water interfaces togive high particulate concentrations in the fuel. Availablebiocides are soluble in both the fuel and water or in the waterphase only.X2.5Tests for Fuel QualityX2.5.1At the time of manufacture, the storage stability ofB6toB20maybeassessedusingTest MethodEN 14112.Othertestsmethodsareunderdevelopment. However, theseacceleratedstabilitytests maynot correlate well witheldstoragestabilityduetovaryingeldconditions andtofuelcomposition.X2.5.2Performance criteria for acceleratedstabilityteststhat ensuresatisfactorylong-termstorageof fuels havenotbeen established.X2.5.3Test Method D 6468 provides an indication of ther-mal oxidative stability of middle distillate fuels when heated totemperatures near 150C.X2.6Fuel MonitoringX2.6.1Aplan for monitoring the quality of bulk fuel duringprolonged storage is an integral part of a successful program. Aplantoreplace agedfuel withfreshproduct at establishedintervals is also desirable.X2.6.2 Stored fuel should be periodically sampled and itsquality assessed. Practice D 4057 provides guidance for sam-pling. Fuel contaminants and degradation products will usuallysettle to the bottomof a quiescent tank. ABottom orD 7467 09a6Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.Clearance sample, as dened in Practice D 4057, should beincluded in the evaluation along with an All Level sample.X2.6.3The quantity of insoluble fuel contaminants presentin fuel can be determined using Test Method D 6217 althoughno precision or bias testing has been performed with B6 to B20blends.X2.6.4Test Method D 6468 can be used for investigation ofoperational problems that might be relatedtofuel thermalstability. Testingsamples fromthe fuel tankor frombulkstorage may give an indication as to the cause of lterplugging. It is more difficult to monitor the quality of fuels invehicletankssinceoperationmaybeonfuelsfrommultiplesources.X2.6.5 Someadditives exhibit effects onfuels testedinaccordance with Test Method D 6468 that may or may not beobserved in the eld. Data have not been developed thatcorrelate results from the test method for various engine typesand levels of operating severity.X2.6.6Ongoing monitoring of the acid number is a usefulmeans of monitoringoxidationor degradationof biodieselblends.X2.7Fuel Storage ConditionsX2.7.1 Contaminationlevels infuel canbe reducedbystorageintankskeptfreeofwater, andtankageshouldhaveprovisions for water draining on a scheduled basis. Waterpromotes corrosion, and microbiological growth may occur ata fuel-water interface. Refer to Guide D 6469 for a morecomplete discussion. Underground storage is preferred to avoidtemperatureextremes; above-groundstoragetanksshouldbeshelteredor paintedwithreectivepaint. Highstoragetem-peratures accelerate fuel degradation. Fixed roof tanks shouldbe kept full to limit oxygen supply and tank breathing.X2.7.2Copper and copper-containing alloys should beavoided. Coppercanpromotefueldegradationandmaypro-ducemercaptidegels. Zinccoatingscanreact withwaterororganic acids in the fuel to form gels that rapidly plug lters.X2.7.3Appendix X2 of Specication D 2880 discusses fuelcontaminants as a general topic.X2.8Fuel Use ConditionsX2.8.1Many diesel engines are designed so that the dieselfuel is usedfor heat transfer. Inmodernheavy-dutydieselengines, for example, only a portion of the fuel that iscirculated to the fuel injectors is actually delivered to thecombustionchamber.Theremainderofthefuel iscirculatedback to the fuel tank, carrying heat with it. Thus adequate hightemperaturestabilitycanbeanecessaryrequirementinsomesevere applications or types of service.X2.8.2Inadequatehightemperaturestabilitymayresultinthe formation of insoluble degradation products.X2.9Use of Degraded FuelsX2.9.1Fuels that have undergone mild-to-moderate degra-dation can sometimes be consumed in a normal way, depend-ing on the fuel system requirements. Filters and other cleanupequipment can require special attention and increased mainte-nance. Burner nozzle or injector fouling can occur morerapidly.X2.9.2Fuels containing very large quantities of fuel degra-dation products and other contaminants or with runawaymicrobiological growth require special attention. Consultationwith experts in this area is desirable. It can be possible to drainthe sediment or draw off most of the fuel above the sedimentlayer and use it with the precautions described in X2.9.1.However, very high soluble gum levels or corrosion productsfrommicrobiological contaminationcancausesevereopera-tional problems.X2.10Thermal Stability GuidelinesX2.10.1Resultsfromtruckeet experiencesuggeststhatTest Method D 6468 can be used to qualitatively indicatewhether diesel fuels have satisfactory thermal stability perfor-mance properties.6,7X2.10.2Performanceinengineshasnot beensufficientlycorrelatedwithresultsfromTest MethodD 6468toprovidedenitivespecicationrequirements. However, thefollowingguidelines are suggested.X2.10.2.1FuelsgivingaTest MethodD 6468reectancevalueof 70%or moreina90minutetest at thetimeofmanufactureshouldgivesatisfactoryperformanceinnormaluse.X2.10.2.2FuelsgivingaTest MethodD 6468reectancevalueof 80%or moreina180minutetest at thetimeofmanufactureshouldgivesatisfactoryperformanceinsevereuse.X2.10.3Thermal stabilityas determinedbyTest MethodD 6468is knowntodegradeduringstorage.8Theguidanceunder X2.10 is for fuels used within six months ofmanufacture.6Bacha, JohnD., andLesnini, DavidG., Diesel Fuel Thermal Stabilityat300F, Proceedings of the 6th International Conference on Stability and Handlingof Liquid Fuels, Vancouver, B.C., October 1997.7Schwab, Scott D., Henly, TimothyJ., Moxley, Joel F., andMiller, Keith,Thermal Stability of Diesel Fuel, Proceedings of the 7th International Conferenceon Stability and Handling of Liquid Fuels, Graz, Austria, September 2000.8Henry, C. P., The du Pont F21 149C (300F) Accelerated Stability Test,Distillate Fuel Stability and Cleanliness, ASTM STP 751 , Stavinoha, L. L., Henry,C. P., editors, ASTM International, W. Conshohocken, PA, 1981, pp. 22-33.D 7467 09a7Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.X3. TENTH PERCENTILE MINIMUM AMBIENT AIR TEMPERATURES FOR THE UNITED STATES(EXCEPT HAWAII)X3.1IntroductionX3.1.1 The tenthpercentile minimumambient air tem-peratures shown on the following maps (Figs. X3.1-X3.12) andinTable X3.1were derivedfromananalysis of historicalhourly temperature readings recorded over a period of 15 to 21years from345weather stations intheUnitedStates. ThisstudywasconductedbytheU.S. ArmyMobilityEquipmentResearchandDevelopment Center (USAMERDC), Coatingand Chemical Laboratory, Aberdeen Proving Ground, MD21005. The tenth percentile minimum ambient air temperatureis dened as the lowest ambient air temperature which will notgolower onaveragemorethan10 %of thetime. Inotherwords,thedailyminimumambientairtemperaturewouldonaverage not be expected to go belowthe monthly tenthpercentile minimum ambient air temperature more than 3 daysfor a 30-day month. See Table X3.1.X3.1.2These data may be used to estimate low temperatureoperabilityrequirements.Inestablishinglowtemperatureop-erabilityrequirements, considerationshouldbegiventothefollowing. Thesefactors,oranycombination,maymakelowtemperatureoperabilitymoreorlessseverethannormal.AsX3.1.2.1throughX3.1.2.12indicate,eldworksuggeststhatcloud point (or wax appearance point) is a fair indication of thelowtemperatureoperabilitylimit of fuelswithout coldowadditives inmost vehicles withdiesel fuel that contains nobiodiesel, and its relevance with B6 to B20 blends has not beenvalidated.X3.1.2.1Longtermweatherpatterns(Averagewinterlowtemperatures will be exceeded on occasion).X3.1.2.2Short term local weather conditions (Unusual coldperiods do occur).X3.1.2.3Elevation(Highlocationsareusuallycolderthansurrounding lower areas).X3.1.2.4Specic engine design.X3.1.2.5Fuel systemdesign(Recyclerate, lterlocation,lter capacity, lter porosity, and so forth.)X3.1.2.6Fuel viscosity at low temperatures.X3.1.2.7Equipment add-ons (Engine heaters, radiator cov-ers, fuel line and fuel lter heaters and so forth.)X3.1.2.8Types of operation (Extensive idling, engine shut-down, or unusual operation).X3.1.2.9Low temperature ow improver additives in fuel.X3.1.2.10Geographic area for fuel use and movementbetween geographical areas.X3.1.2.11General housekeeping (Dirt or water, or both, infuel or fuel supply system).FIG. X3.1 October10th Percentile Minimum TemperaturesD 7467 09a8Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.X3.1.2.12Impact failure for engine to start or run (Criticalvs. non-critical application).X3.1.3Historical BackgroundThree test methods havebeen widely used to estimate or correlate with low temperaturevehicle operability with diesel fuel that contains no biodiesel.These test methods may be useful to estimate or correlate withlower temperature vehicle operability with B6 to B20, but theiruse with B6 to B20 has not been validated. Cloud point, TestMethod D 2500, is the oldest of the three and most conserva-tiveof thetests. Thecloudpoint test indicates theearliestappearance of wax precipitation that might result in pluggingof fuel lters or fuel lines under prescribed cooling conditions.Although not 100 % failsafe, it is the most appropriate test forapplicationsthat cannot toleratemuchrisk. TheColdFilterPluggingPoint (CFPP)test, Test MethodD 6371, wasintro-duced in Europe in 1965. The CFPP was designed to correlatewiththemajorityofEuropeanvehicles. Underrapidcoolingconditions, 20 cc fuel is drawn through a 45 micron screen thenallowedtoowbackthroughthescreenforfurthercooling.This process is continued every 1C until either the 20 cc fuelfails to be drawn through the screen in 60 s or it fails to returnthroughthescreenin60s. ItwaseldtestedmanytimesinEurope9beforebeingwidelyacceptedasaEuropeanspeci-cation. FieldtestshavealsoshownCFPPresultsmorethan10Cbelowthecloudpoint shouldbeviewedwithcautionbecause those results did not necessarily reect the true vehiclelow temperature operability limits.10CFPP has been applied tomanyareas of theworldwheresimilar vehicledesigns areused.TheLowTemperatureFlowTest (LTFT),Test MethodD 4539, was designed to correlate with the most severe and oneof the most common fuel delivery systems used in NorthAmerican Heavy Duty trucks. Under prescribed slowcoolconditions(1C/h),similartotypicaleldconditions,several200ccfuel specimensinglasscontainersttedwith17mscreen assemblies are cooled. At 1C intervals one specimen isdrawnthroughthescreenundera20kPavacuum. Approxi-mately 90 % of the fuel must come over in 60 s or less for theresult to be a pass. This process is continued at lowertemperatures (1C increments) until the fuel fails to come overin the allotted 60 s. The lowest passing temperature is denedas the LTFTfor that fuel. In 1981, a CRCprogramwasconducted to evaluate the efficacy of cloud point, CFPP, pourpoint, and LTFT for protecting the diesel vehicle population inNorth America and to determine what benet ow-improverscould provide. The eld test consisted of 3 non-ow improveddiesel fuels, 5 ow improved diesel fuels, 4 light-duty passen-ger cars, and 3 heavy-duty trucks. The eld trial resulted in two9LowTemperatureOperabilityof Diesels. AReport byCECInvestigationGroup IGF-3, CEC, P-171-82.10SFPPA NewLaboratory Testfor AssessmentofLow TemperatureOper-ability of Modern Diesel Fuels, CEC/93/EF 15, May 1993, pp. 5-7.FIG. X3.2 November10th Percentile Minimum Ambient Air TemperaturesD 7467 09a9Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.documents11,12that provide insight into correlating laboratorytests to North American vehicle performance in the eld. Thegeneral conclusions of the study were:(1) In overnight cool down, 30 % of the vehicles tested hada nal fuel tank temperature within 2Cof the overnightminimum ambient temperature.(2) Theuseof ow-improveddiesel fuel permits somevehicles to operate well below the fuel cloud point.(3) Signicant differencesexist intheseverityof dieselvehicles in terms of low temperature operation.(4) Nosinglelaboratorytest was foundthat adequatelypredicts the performance of all fuels in all vehicles.(5) CFPP was a better predictor than pour point, but bothmethodsover-predicted, minimumoperatingtemperaturesinmany vehicles. For this reason, these tests were judgedinadequate predictors of low-temperature performance anddismissed from further consideration.(6) Cloud point and LTFTshowed varying degrees ofpredictive capability, and offered distinctively different advan-tages.Bothpredictedtheperformanceofthebasefuelswell,but LTFTmoreaccuratelypredictedtheperformanceof theow-improvedfuels. Onthe other hand, cloudpoint cameclosesttoafail-safepredictorofvehicleperformanceforallvehicles.Sincethe1981eldtest, non-independent studies13usingnewervehiclesveriedthesuitabilityoftheLTFTforNorthAmerican heavy-duty trucks. Users are advised to review theseand any more recent publications when establishing lowtemperatureoperabilityrequirementsanddecidingupontestmethods.X3.1.3.1CurrentPracticesItisrecognizedthatfueldis-tributors, producers, andendusersintheUnitedStatesusecloud point, wax appearance point, CFPP, and LTFT toestimatevehiclelowtemperatureoperabilitylimitsfordieselfuel. No independent data has been published in recent years todetermine test applicability for todays fuels and vehicles.X3.2MapsX3.2.1The maps in the following gures were derived fromCCL Report No. 316, APredictive Study for DeningLimitingTemperatures andTheir Application in PetroleumProduct Specications,byJohnP. Doner. This report waspublished by the U.S. Army Mobility Equipment Research andDevelopment Center (USAMERDC), CoatingandChemicalLaboratory, andit is availablefromtheNational Technical11CRC Report No. 537, The Relationship Between Vehicle Fuel Temperatureand Ambient Temperature, 1981 CRC Kapuskasing Field Test, December 1983.12CRC Report No. 528, 1981 CRC Diesel Fuel Low-Temperature OperabilityField Test, September 1983.13SAE 962197, SAE 982576, SAE 2000012883.FIG. X3.3 December10th Percentile Minimum Ambient Air TemperaturesD 7467 09a10Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.Information Service, Springeld, VA22151, by requestingPublication No. AD0756420.X3.2.2Where states are divided the divisions are noted onthe maps and table with the exception of California, which isdivided by counties as follows:California, North CoastAlameda, Contra Costa, DelNorte, Humbolt, Lake, Marin, Mendocino, Monterey, Napa,SanBenito, SanFrancisco, SanMateo, Santa Clara, SantaCruz, Solano, Sonoma, Trinity.California, InteriorLassen, Modoc, Plumas, Sierra,Siskiyou, Alpine, Amador, Butte, Calaveras, Colusa, El Do-rado, Fresno, Glenn, Kern (except that portion lying east of theLos Angeles CountyAqueduct), Kings, Madera, Mariposa,Merced,Placer,Sacramento,SanJoaquin,Shasta,Stanislaus,Sutter, Tehama, Tulare, Tuolumne, Yolo, Yuba, Nevada.California, South CoastOrange, San Diego, San LuisObispo, Santa Barbara, Ventura, Los Angeles (except thatportion north of the San Gabriel Mountain range and east of theLos Angeles County Aqueduct).California, SoutheastImperial, Riverside, San Bernardino,Los Angeles(thatportionnorthoftheSanGabrielMountainrangeandeastoftheLos AngelesCounty Aqueduct),Mono,Inyo, Kern (that portion lying east of the Los Angeles CountyAqueduct).X3.2.3ThetemperaturesinCCLReport No. 316wereindegreesFahrenheit. ThedegreeCelsiustemperaturesinAp-pendixX3wereobtainedbyconvertingtheoriginal degreeFahrenheit temperatures.FIG. X3.4 January10th Percentile Minimum Ambient Air TemperaturesD 7467 09a11Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.FIG. X3.5 February10th Percentile Minimum Ambient Air TemperaturesD 7467 09a12Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.FIG. X3.6 March10th Percentile Minimum Ambient Air TemperaturesFIG. X3.7 October10th Percentile Minimum Ambient Air TemperaturesD 7467 09a13Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.FIG. X3.8 November10th Percentile Minimum Ambient Air TemperaturesFIG. X3.9 December10th Percentile Minimum Ambient Air TemperaturesD 7467 09a14Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.FIG. X3.10 January10th Percentile Minimum Ambient Air TemperaturesFIG. X3.11 February10th Percentile Minimum Ambient Air TemperaturesD 7467 09a15Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.FIG. X3.12 March10th Percentile Minimum Ambient Air TemperaturesD 7467 09a16Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.TABLE X3.1Tenth Percentile Minimum Ambient Air Temperatures for the United States (except Hawaii)State10th Percentile TemperatureC, minOct. Nov. Dec. Jan. Feb. MarchAlabama 4 3 6 7 3 2Alaska Northern 25 37 45 49 47 43Southern 11 13 18 32 32 29South East 4 11 16 19 13 12Arizona North 34 latitude 4 12 14 17 16 12South 34 latitude 7 0 2 4 3 1Arkansas 2 4 7 11 7 3California North Coast 3 0 2 2 1 1Interior 2 3 4 7 6 6South Coast 6 2 0 1 0 2Southeast 1 6 8 11 7 5Colorado East 105 long 2 12 14 19 15 12West 105 long 8 18 25 30 24 16Connecticut 1 7 16 17 16 9Delaware 2 3 10 11 10 6Florida North 29 latitude 7 1 2 3 1 2South 29 latitude 14 7 3 3 5 7Georgia 3 2 6 7 6 2Idaho 4 13 18 21 18 13Illinois North 40 latitude 1 9 19 21 18 11South 40 latitude 1 7 16 17 15 8Indiana 1 7 16 18 16 9Iowa 2 13 23 26 22 16Kansas 2 11 15 19 14 13Kentucky 1 6 13 14 11 6Louisiana 5 1 3 4 2 1Maine 3 10 23 26 26 18Maryland 2 3 10 12 10 4Massachusetts 2 7 16 18 17 10Michigan 2 11 20 23 23 18Minnesota 4 18 30 34 31 24Mississippi 3 3 6 6 4 1Missouri 1 7 14 16 13 8Montana 7 18 24 30 24 21Nebraska 3 13 18 22 19 13Nevada North 38 latitude 7 14 18 22 18 13South 38 latitude 8 0 3 4 2 1New Hampshire 3 8 18 21 21 12New Jersey 2 3 11 12 11 6New Mexico North 34 latitude 2 11 14 17 14 11South 34 latitude 4 4 8 11 7 3New York North 42 latitude 3 8 21 24 24 16South 42 latitude 1 5 14 16 15 9North Carolina 1 7 10 11 9 5North Dakota 4 20 27 31 29 22Ohio 1 7 16 17 15 9Oklahoma 1 8 12 13 8 7Oregon East 122 long 6 11 14 19 14 9West 122 long 0 4 5 7 4 3Pennsylvania North 41 latitude 3 8 19 20 21 15South 41 latitude 0 6 13 14 14 8Rhode Island 1 3 12 13 13 7South Carolina 5 1 5 5 3 2South Dakota 4 14 24 27 24 18Tennessee 1 5 9 11 9 4Texas North 31 latitude 3 6 9 13 9 7South 31 latitude 9 2 2 3 1 2Utah 2 11 14 18 14 8Vermont 3 8 20 23 24 15Virginia 2 3 9 11 9 4Washington East 122 long 2 8 11 18 11 8West 122 long 0 3 3 7 4 3West Virginia 3 8 15 16 14 9Wisconsin 3 14 24 28 24 18Wyoming 4 15 18 26 19 16D 7467 09a17Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.SUMMARY OF CHANGESSubcommitteeD02.E0hasidentiedthelocationofselectedchangestothisstandardsincethelast issue(D 7467 09) that may impact the use of this standard. (Approved April 15, 2009.)(1) AddedTest MethodD 7397cloudpoint asanoptiontoTest Method D 2500 in 4.1.3 and to Referenced Documents.SubcommitteeD02.E0hasidentiedthelocationofselectedchangestothisstandardsincethelast issue(D 7467 08) that may impact the use of this standard. (Approved March 1, 2009.)(1) Replaced wording in X1.15.ASTM International takes no position respecting the validity of any patent rights asserted in connection with any item mentionedin this standard. Users of this standard are expressly advised that determination of the validity of any such patent rights, and the riskof infringement of such rights, are entirely their own responsibility.This standard is subject to revision at any time by the responsible technical committee and must be reviewed every ve years andif not revised, either reapproved or withdrawn. Your comments are invited either for revision of this standard or for additional standardsand should be addressed to ASTM International Headquarters. Your comments will receive careful consideration at a meeting of theresponsible technical committee, which you may attend. If you feel that your comments have not received a fair hearing you shouldmake your views known to the ASTM Committee on Standards, at the address shown below.This standard is copyrighted by ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959,UnitedStates. Individual reprints(singleormultiplecopies)of thisstandardmaybeobtainedbycontactingASTMat theaboveaddress or at 610-832-9585 (phone), 610-832-9555 (fax), or [email protected] (e-mail); or through the ASTMwebsite(www.astm.org).D 7467 09a18Copyright by ASTM Int'l (all rights reserved); Thu Oct 15 13:27:56 EDT 2009Downloaded/printed byStephen Martin (Martin Eagle Oil Company, Inc.) pursuant to License Agreement. No further reproductions authorized.