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本文(ASTM D3427-2006 Standard Test Method for Air Release Properties of Petroleum Oils《石油脱气特性的标准试验方法》.pdf)为本站会员(hopesteam270)主动上传,麦多课文库仅提供信息存储空间,仅对用户上传内容的表现方式做保护处理,对上载内容本身不做任何修改或编辑。 若此文所含内容侵犯了您的版权或隐私,请立即通知麦多课文库(发送邮件至master@mydoc123.com或直接QQ联系客服),我们立即给予删除!

ASTM D3427-2006 Standard Test Method for Air Release Properties of Petroleum Oils《石油脱气特性的标准试验方法》.pdf

1、Designation: D 3427 06Designation 31301An American National StandardStandard Test Method forAir Release Properties of Petroleum Oils1This standard is issued under the fixed designation D 3427; the number immediately following the designation indicates the year oforiginal adoption or, in the case of

2、revision, the year of last revision. A number in parentheses indicates the year of last reapproval. Asuperscript epsilon (e) indicates an editorial change since the last revision or reapproval.1. Scope1.1 This test method covers the ability of turbine, hydraulic,and gear oils to separate entrained a

3、ir.NOTE 1This test method was developed for mineral based oils. It maybe used for some synthetic fluids; however, the precision statement appliesonly to petroleum oils.1.2 This standard does not purport to address all of thesafety concerns, if any, associated with its use. It is theresponsibility of

4、 the user of this standard to establish appro-priate safety and health practices and determine the applica-bility of regulatory limitations prior to use.2. Referenced Documents2.1 ASTM Standards:2D 1193 Specification for Reagent WaterD 1401 Test Method for Water Separability of PetroleumOils and Syn

5、thetic FluidsE1 Specification for ASTM Liquid-in-Glass Thermometers2.2 DIN Standard:3DIN 51 3813. Terminology3.1 Definitions of Terms Specific to This Standard:3.1.1 air release time, nthe number of minutes needed forair entrained in the oil to reduce in volume to 0.2 % under theconditions of this t

6、est and at the specified temperature.4. Summary of Test Method4.1 Compressed air is blown through the test oil, which hasbeen heated to a temperature of 25, 50, or 75C. After the airflow is stopped, the time required for the air entrained in the oilto reduce in volume to 0.2 % is recorded as the air

7、 release time.NOTE 2By agreement between the customer and the laboratory, theoil may be heated at other temperatures. However, the precision at thesedifferent temperatures is not known at present.5. Significance and Use5.1 Agitation of lubricating oil with air in equipment, suchas bearings, coupling

8、s, gears, pumps, and oil return lines, mayproduce a dispersion of finely divided air bubbles in the oil. Ifthe residence time in the reservoir is too short to allow the airbubbles to rise to the oil surface, a mixture of air and oil willcirculate through the lubricating oil system. This may result i

9、nan inability to maintain oil pressure (particularly with centrifu-gal pumps), incomplete oil films in bearings and gears, andpoor hydraulic system performance or failure.5.2 This test method measures the time for the entrained aircontent to fall to the relatively low value of 0.2 % volumeunder a st

10、andardized set of test conditions and hence permitsthe comparison of the ability of oils to separate entrained airunder conditions where a separation time is available. Thesignificance of this test method has not been fully established.However, entrained air can cause sponginess and lack ofsensitivi

11、ty of the control of turbine and hydraulic systems. Thistest may not be suitable for ranking oils in applications whereresidence times are short and gas contents are high.6. Apparatus6.1 Aschematic diagram of the apparatus is shown in Fig. 1.The component parts are described as follows:6.1.1 Test Ve

12、ssel, made of borosilicate glass as shown in Fig.2, consisting of a jacketed sample tube fitted with an air inletcapillary, baffle plate, and air outlet tube. The two parts of eachtest vessel should be marked and preferably used as a pair.Interchanged parts may be used so long as the resultant testv

13、essel conforms to the stated dimensions.6.1.2 Pressure Gage, covering the range from 0 to 35 kPa,with divisions at least every 2 kPa, and an accuracy of 1.5 kPa.6.1.3 Thermometers:1This test method is under the jurisdiction of ASTM Committee D02 onPetroleum Products and Lubricants and is the direct

14、responsibility of SubcommitteeD02.C0 on Turbine Oils.Current edition approved July 1, 2006. Published August 2006. Originallyapproved in 1975. Last previous edition approved in 2003 as D 342703.Adopted as a joint ASTM/IP standard in 2006.2For referenced ASTM standards, visit the ASTM website, www.as

15、tm.org, orcontact ASTM Customer Service at serviceastm.org. For Annual Book of ASTMStandards volume information, refer to the standards Document Summary page onthe ASTM website.3Available from Beuth Verlag GmbH, Burggrafenstrasse 6, 1000 Berlin 30,Germany.1Copyright ASTM International, 100 Barr Harb

16、or Drive, PO Box C700, West Conshohocken, PA 19428-2959, United States.6.1.3.1 Air Thermometer, for measuring compressed airtemperature. ASTM Precision Thermometer having a rangefrom 20 to 102C, graduated in 0.2C and conforming to therequirements for Thermometer 12C as prescribed in Specifi-cation E

17、1is suitable. A temperature sensor of at least equiva-lent performance is also suitable. Care shall be taken to avoidrestricting the air path with the thermometer bulb or anyadapter used.6.1.3.2 Sample Thermometer, for measuring the tempera-ture of the sample during preparation and trial runs. ASTMP

18、recision Thermometer having a range from 20 to 102C,graduated in 0.2C and conforming to the requirements forThermometer 12C as prescribed in Specification E1is suit-able.Atemperature sensor of at least equivalent performance isalso suitable.6.1.4 Heater, to bring the compressed air up to measure-men

19、t temperature. A coil of copper tubing immersed in thecirculating bath (see 6.1.5) is suitable at 25C, but additionalheating is necessary at 50 and 75C.This can be obtained by anadditional bath, or by using a separate steam or electric heatexchanger. The temperature of the air shall be measured by a

20、thermometer located as close as possible to the testing vesseland meeting the specifications shown in 6.1.3.NOTE 3The application of thermal insulation to the pipework carry-ing the heated compressed air is recommended.6.1.5 Circulating Bath, approximately 10-L capacity with arate of flow of 10 L/mi

21、n and capable of maintaining the test cellat a temperature of 25, 50, or 75C within 60.1C.NOTE 4Use of water in the bath has been found to minimizeelectrostatic effects.NOTE 5The application of thermal insulation to the pipework carry-ing the heated bath fluid is recommended.(WarningThe use of glass

22、 vessels with glass host fittingsfor circulating 75C (167F) bath medium is potentiallydangerous. Back pressure in excess of a gage pressure of 70kPa (10 psi) can be generated when the bath medium ispumped at the required rate; this can cause fracture of the glassor slippage of the hose connections.

23、Use of a pressure reliefvalve set at 70 kPa (10 psi) is recommended. In addition, useof a safety shield is recommended.)6.2 Balance, capable of measuring density, accurate to 0.5kg/m3.6.3 Sinker, having a round or tapered bottom of 5 or 10-mLdisplacement, 80.0 6 1.5-mm length. If the sinker contains

24、 athermometer, it shall be usable between 25 and 75C.6.4 Oven, capable of heating samples to 10C above the testtemperature.6.5 Timer, readable to 0.1 min, with an accuracy of betterthan 0.1 %.6.6 Pump, with a nonpulsating output and capable ofmaintaining an air flow of 40 L/min at a pressure of 20 k

25、Pa(optional, see 7.4).7. Materials7.1 Purity of ReagentsReagent grade chemicals shall beused in all tests. Unless otherwise indicated, it is intended thatall reagents conform to the specifications of the Committee onAnalytical Reagents of the American Chemical Society wheresuch specifications are av

26、ailable.4Other grades may be used,provided it is first ascertained that the reagent is of sufficientlyhigh purity to permit its use without lessening the accuracy ofthe determination.7.2 Purity of WaterReagent water as defined by Type II ofSpecification D 1193.7.3 Acetone, minimum reagent grade. (Wa

27、rningFlammable. Health hazard.)7.4 Air, Compressed, dry and free from moisture, particu-lates, and oil. Air from a cylinder or a nonpulsating pump maybe used. (WarningCompressed gas under high pressure.)7.5 Cleaning Reagent, Cleaning either in hot Nochromix5(WarningCorrosive health hazard oxidizer),

28、 or a 24-h soakat room temperature in Micro6solution.NOTE 6Previously, chrome sulfuric acid was used in this procedure.Other test methods (for example, Test Method D 1401) have demonstratedacceptable, statistically equivalent results when Nochromix or Micro isused to replace sulfuric chromic acid fo

29、r cleaning.7.6 n-Heptane, reagent grade. (WarningFlammable.Harmful if inhaled.)4Reagent Chemicals, American Chemical Society Specifications, AmericanChemical Society, Washington, DC. For suggestions on the testing of reagents notlisted by the American Chemical Society, see Analar Standards for Labor

30、atoryChemicals, BDH Ltd., Poole, Dorset, U.K., and the United States Pharmacopeiaand National Formulary, U.S. Pharmacopeial Convention, Inc. (USPC), Rockville,MD.5The sole source of supply of Nochromix known to the committee at this timeis Godax Laboratories, Inc., 720-B Erie Ave., Takoma Park, MD 2

31、0912. If you areaware of alternative suppliers, please provide this information to ASTM Interna-tional Headquarters. Your comments will receive careful consideration at a meetingof the responsible technical committee,1which you may attend.6The sole source of supply of Micro known to the committee at

32、 this time isInternational Products Corp., P.O. Box 70, Burlington, NJ 08016. If you are awareof alternative suppliers, please provide this information to ASTM InternationalHeadquarters. Your comments will receive careful consideration at a meeting of theresponsible technical committee,1which you ma

33、y attend.FIG. 1 Apparatus for the Determination of Air Release TimeD3427062NOTE 7Other alternate solvents, such as toluene, etc., may be used inplace of n-heptane.8. Preparation of Apparatus8.1 Clean the interior of the test vessel, including the airinlet and sinker, and all other glassware coming i

34、n contact withthe sample, before each determination in the following manner:8.1.1 Rinse away the oil residue with n-heptane(Warningsee 7.6) and acetone (Warningsee 7.3) and dryby air blowing.8.1.2 Clean the apparatus by immersing in cleaning reagentin order to remove completely any traces of silicon

35、e.8.1.3 Rinse with reagent water.FIG. 2 Test VesselD34270638.1.4 Rinse with acetone (Warningsee 7.3) and dry withclean compressed air (Warningsee 7.4).NOTE 8Oil misting occurs during blowing. The test vessel should bein a hood, or the air outlet tube should be connected to a vent that removesthe vap

36、ors.9. Procedure9.1 Assemble the test apparatus as shown in Fig. 1. Set thecompressed air temperature to within 0.2C of the desired testtemperature. Set the circulating bath to give a specimentemperature within 0.1C of the desired test temperature. Therequired bath temperature setting and time for t

37、he specimen toequilibrate can be established for an equipment setup bymaking trial runs with a thermometer in the oil specimen. Foroils with a viscosity at 40C of less than 9.0 cSt, the testtemperature shall be 25C. For oils with a viscosity at 40Cbetween 9.0 and 90 cSt, the test temperature shall b

38、e 50C. Oilshaving a viscosity at 40C greater than 90 cSt shall be tested at75C.9.2 Warm approximately 200 mLof the oil to be tested in anoven set at a temperature of 10C higher than the testtemperature.9.3 Pour 180 6 5 mL of the heated sample into the testvessel.9.4 Allow the sample to equilibrate t

39、o the desired testtemperature, using the heating-up time previously established(see 9.1) or by directly measuring the temperature.9.5 Warm the sinker of the balance to the test temperature inan air bath, such as a glass cylinder fitted with a suitable coversituated in the circulating bath. When the

40、sinker has reachedthe test temperature, immerse it in the sample, taking care thatno air bubbles cling to it. Attach the sinker to the beam of thedensity balance by means of the platinum wire so that thebottom of the sinker is 10 6 2 mm from the bottom of the testvessel.NOTE 9The sinker can take app

41、roximately 20 min to reach 50C or 35min to reach 75C.9.6 Allow the density reading to stabilize, read the densityfrom the balance to the nearest 0.1 kg/m3, and record it as theinitial density.9.7 Return the sinker to the air bath and replace it with theair inlet tube as shown in Fig. 2. After 5 min,

42、 start the supplyof air at a gage pressure of 20 kPa at the required temperature.Maintain the pressure and temperature of the air (25, 50, and75C) by readjustments, if necessary.9.8 After 7 6 0.1 min, shut off the air and immediately startthe timer. Quickly remove the inlet tube from the test vessel

43、,and immerse the sinker in the oil/air dispersion.Attach the wireto the beam and maintain a distance of 10 6 2 mm between thebottom of the sinker and the bottom of the test vessel.NOTE 10In the case of certain oils, which form a considerable volumeof oil/air dispersion, the top of the sinker can ini

44、tially be in foam, andhence, density readings at this time can be in error.9.9 Record the time, to the nearest 0.1 min, for the densityto return to the target of 99.8 % of the initial density (d0). If thetime is greater than 30 min, discontinue the test.NOTE 11The test may be run for a longer period

45、 of time by agreementbetween the laboratory and the customer.NOTE 12For some applications, the shape of the air release time curvemay be required. This can be implemented by recording the density atintervals, as required.9.10 Certain oils may lose light components during the airsaturation, thus chan

46、ging their effective density. This will benoted if the time for the density to return to the initial figure isinstantaneous. Where air release value information is requiredfor such oils, an air releasing time curve may be drawn. If theloss causes any part of the sinker to be exposed, discontinue the

47、test and repeat, using a sample that is 10 mL larger thanpreviously used.10. Calculation of Density10.1 Density:Density of sample kg/m3!5 (1)Weight of sinker in air kg! Weight of sinker in sample kg!#Volume of sinker m3!NOTE 13A 10 mL sinker has a volume of 10 3 10-6m3.10.2 Target Density:Initial de

48、nsity d0!30.998. (2)10.3 If the tare key of the balance is pressed while the sinkeris being weighed in air so that the reading is zeroed, then thefollowing may be used:Density of sample kg/m3!5Weight of sinker in sample kg!Volume of sinker m3!(3)NOTE 14Some instruments automatically make the above c

49、alcula-tions.10.4 The volume of the sinker may be determined byweighing it in air, then in water. The difference in weight (kg)3 103= volume in m3.11. Reporting11.1 Report the air release time, as recorded in 9.9, and thetest temperature in C.12. Precision and Bias7NOTE 15The program was run by six laboratories, using five samplesof unused steam turbine oils and base stocks with air used as the entrainedgas. Five samples were tested at one temperature and four at another.Since some reports were incomplete, this result

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