ASTM D7043-2010 5625 Standard Test Method for Indicating Wear Characteristics of Petroleum and Non-Petroleum Hydraulic Fluids in a Constant Volume Vane Pump《指示在恒容量叶片泵中石油和非石油液压流体的耐用.pdf

《ASTM D7043-2010 5625 Standard Test Method for Indicating Wear Characteristics of Petroleum and Non-Petroleum Hydraulic Fluids in a Constant Volume Vane Pump《指示在恒容量叶片泵中石油和非石油液压流体的耐用.pdf》由会员分享，可在线阅读，更多相关《ASTM D7043-2010 5625 Standard Test Method for Indicating Wear Characteristics of Petroleum and Non-Petroleum Hydraulic Fluids in a Constant Volume Vane Pump《指示在恒容量叶片泵中石油和非石油液压流体的耐用.pdf（12页珍藏版）》请在麦多课文档分享上搜索。

1、Designation: D7043 10Standard Test Method forIndicating Wear Characteristics of Non-Petroleum andPetroleum Hydraulic Fluids in a Constant Volume VanePump1This standard is issued under the fixed designation D7043; the number immediately following the designation indicates the year oforiginal adoption

2、 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*1.1 This test method covers a constant volume vane pumptest procedure operated

3、at 1200 rpm and 13.8 MPa.1.2 The values stated in SI units are to be regarded asstandard. No other units of measurement are included in thisstandard.1.2.1 ExceptionThere are no SI equivalents for the inchfasteners and inch O-rings that are used in the apparatus in thistest method.1.2.2 ExceptionIn s

4、ome cases English pressure values aregiven in parentheses as a safety measure.1.3 This standard does not purport to address all of thesafety concerns, if any, associated with its use. It is theresponsibility of the user of this standard to establish appro-priate safety and health practices and deter

5、mine the applica-bility of regulatory limitations prior to use.2. Referenced Documents2.1 ASTM Standards:2D2882 Test Method for Indicating Wear Characteristics ofPetroleum and Non-Petroleum Hydraulic Fluids in Con-stant Volume Vane Pump3D6300 Practice for Determination of Precision and BiasData for

6、Use in Test Methods for Petroleum Products andLubricantsE691 Practice for Conducting an Interlaboratory Study toDetermine the Precision of a Test Method3. Terminology3.1 Definitions of Terms Specific to This Standard:3.1.1 flushing, vprocess of cleaning the test system beforetesting to prevent cross

7、-contamination.3.1.2 torquing, vprocess of tightening the pump headbolts to achieve a uniform clamping force.4. Summary of Test Method4.1 An amount of 18.9 6 0.5 L of a hydraulic fluid arecirculated through a rotary vane pump system for 100 h at apump speed of 1200 6 60 r/min and a pump outlet press

8、ure of13.8 6 0.3 MPa (2000 6 40 psi). Fluid temperature at thepump inlet is 66 6 3C for all water glycols, emulsions, andother water containing fluids and for petroleum and syntheticfluids of ISO Grade 46 or lighter. A temperature of 80 6 3Cis used for all other synthetic and petroleum fluids.4.2 Th

9、e result obtained is the total mass loss from the camring and the twelve vanes during the test. Other reported valuesare initial flow rate and final flow rate.4.3 The total quantity of test oil required for a run is 26.5 L.5. Significance and Use5.1 This test method is an indicator of the wear chara

10、cter-istics of non-petroleum and petroleum hydraulic fluids operat-ing in a constant volume vane pump. Excessive wear in vanepumps could lead to malfunction of hydraulic systems incritical applications.6. Apparatus6.1 The basic system consists of the following (see Fig. 1):6.1.1 AC Motor, 1200-rpm,

11、or other suitable drive, with 11kw (15 hp) as suggested minimum power requirement (Item 5,Fig. 1).The motor must have right hand rotation (counterclock-wise rotation as viewed from the shaft end).6.1.2 Test Stand Base, with appropriate, rigid mounting forthe motor, pump, reservoir, and other compone

12、nts.6.1.3 Rotary Vane Pump, replaceable cartridge type. AVickers4V104C or V105C or Conestoga USA B1 housing is1This test method is under the jurisdiction of ASTM Committee D02 onPetroleum Products and Lubricants and is the direct responsibility of SubcommitteeD02.N0 on Hydraulic Fluids.Current editi

13、on approved May 1, 2010. Published September 2010. Originallyapproved in 2004. Last previous edition approved in 2004 as D704304a. DOI:10.1520/D7043-10.2For referenced ASTM standards, visit the ASTM website, www.astm.org, orcontact ASTM Customer Service at serviceastm.org. For Annual Book of ASTMSta

14、ndards volume information, refer to the standards Document Summary page onthe ASTM website.3Withdrawn. The last approved version of this historical standard is referencedon www.astm.org.4Previously available, this apparatus was made obsolete in 2000 by Vickers,which is part of Eaton Hydraulics Group

15、 USA 14615 Lone Oak Road Eden Prairie,MN 55344. If you are aware of alternative suppliers, please provide this informationto ASTM International Headquarters. Your comments will receive careful consid-eration at a meeting of the responsible technical committee,1which you may attend.1*A Summary of Cha

16、nges section appears at the end of this standard.Copyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959, United States.Item Description Required?1. Reservoir2. Inlet temperature sensor3. Pump4. Flexible coupling5. Motor6. High pressure gauge7. Snubber valv

17、e8. Relief valve9. Filter10. Heat exchanger11. Temperature control valve12. Flow meter13. Low pressure gauge14. Fluid sampling port15. Pump inlet valve Not required16. Return line valve Not required17. Inlet vacuum gauge Not required18. Outlet temperature sensor Not required19. Case drain for B1 pum

18、pA. 61 to 66 cm, vertical RequiredB. 15.2 cm, minimum horizontal RequiredC. 10.2 cm, maximum RequiredFIG. 1 System SchematicD7043 102used along with internal components from Conestoga USA,Inc.5The assembly should produce 28.4 L/min flow at 1200r/min with ISO Grade 32 fluid at 49C, at 6.9 MPa (Item 3

19、, Fig.1; Fig. 2; Fig. 3). (WarningEaton-Vickers test pump is ratedat 6.9 MPa (1000 psi) but is being operated at 13.8 MPa (2000psi). A protective shield around the pump is recommended.)NOTE 1This test method has been written for the use of ConestogaUSA Inc. internals along with an Eaton-Vickers or C

20、onestoga USAhousing and head. If components from other manufacturers are used, referto Test Method D288200 for preparation and selection guidelines.6.1.3.1 The replaceable cartridge consists of the cam ring,the rotor, two bushings, a set of twelve vanes, and an alignmentpin.6.1.3.2 The individual ca

21、rtridge parts are purchased sepa-rately. Conestoga USA, Inc. part numbers for these items are:cam ring No. 2882-5, alignment pin No. 2882-10, rotor No.2882-1C, bronze bushings No. 2882-4C and 2882-4E, andvane kit (12 vanes) No. 2882-V12.6.1.3.3 There are to be no modifications to the pumphousing suc

22、h as plugging the drain hole in the pump body ordrilling and tapping a hole in the head for an external drain.6.1.4 Reservoir, (Item 1, Fig. 1).6.1.4.1 The reservoir shall be equipped with a removablebaffle and a close fitting lid, all of stainless steel construction.The reservoir can be square or r

23、ectangular (with a flat bottom)5The sole source of supply of the apparatus known to the committee at this timeis Conestoga USA Inc., P.O. Box 3052, Pottstown, PA 19464. If you are aware ofalternative suppliers, please provide this information to ASTM InternationalHeadquarters. Your comments will rec

24、eive careful consideration at a meeting of theresponsible technical committee,1which you may attend.Description of ItemsItem Number Name Amount Description1 Head Bolt 838-16 3 1-14-in. hex head cap screw, Grade 82 Head Bearing 1 No. 6200, open type3 Pump Head 1 Vickers 240644 Head PackingA1 235 squa

25、re cut O-ring5 Outer Bushing 1 Conestoga 2882-4E6 Alignment Pin 1 Conestoga 2882-107 Cam RingB1 Conestoga 2882-58 RotorB1 Conestoga 2882-1C9 VaneB12 Conestoga 2882-V12 (12 piece kit)10 Inner Bushing 1 Conestoga 2882-4C11 Pump Body 1 Vickers 18823512 Retaining Ring 1 20-mm steel retaining ring 3AM120

26、13 Shaft Bearing 1 #6204, open type14 Seal Retainer 1 Vickers 18507815 O-RingA1 223 O-ring16 Shaft SealA1 double lip with garter spring .875 3 1.500 3 .312 rubber clad17 Shaft 1 Conestoga 2882-2A18 Key 1 Conestoga 2882-20A or Vickers 161219a Foot Mount 1 Vickers 18823419b Flange Mount 1 Vickers 1882

27、3320 Gasket 1Conestoga 2882-27 or Vickers 2546 not used with Foot Mount (item19a)21 Screw 638-16 378 socket head cap screwASpecify compound.BSpecify size.FIG. 2 Pump ComponentsD7043 103or cylindrical (with a spherical or cone shaped bottom) andmust be designed so as to avoid air entrainment in the f

28、luid.NOTE 2A suitable reservoir design is presented in Test MethodD288200.6.1.4.2 To promote deaeration and thermal mixing of thefluid, the baffle shall be designed so that returning fluid willfollow an indirect path from the return port to the outlet port.6.1.4.3 To avoid air entrainment, the reser

29、voir shall bedesigned so that the return line enters well below the fluidlevel, fluid flow does not cascade over the baffle, and there willbe a minimum of 15 cm of fluid depth above the pump inletline.6.1.4.4 Fluid ports may be added as required by the user forthe installation of a low level switch,

30、 reservoir temperaturesensor, bottom drain, and so forth.6.1.4.5 If the reservoir is positioned so that the contentscannot be visually checked for aeration by removing the lid, afluid-tight glass viewing port may be located in the side of thereservoir.6.1.5 Outlet Pressure Control Valve, Eaton-Vicke

31、rs pressurerelief valve (CT-06-C/3.4 to 13.8 MPa) with either manual orremote control (Item 8, Fig. 1).66.1.6 Temperature Control Device, suitable for controllingcoolant flow to the heat exchanger to maintain test fluid at thespecified temperature (Item 11, Fig. 1).6.1.7 Temperature Indicator, (Item

32、 2, Fig. 1) shall have anaccuracy of 61C and shall have an appropriate sensor tomonitor pump inlet temperature.6.1.7.1 To prevent a flow restriction near the pump inletport, the temperature probe shall have a diameter of not morethan 6 mm.6.1.7.2 The test fluid temperature shall be measured within10

33、.2 cm of the pump inlet (Dimension C, Fig. 1). The sensingprobe shall be inserted into the midpoint of flow.NOTE 3Some users have found the addition of a pump outlet6Request Vickers publication I-3369-S for the relief valve service data. Seehttp:/ 3 Conestoga USA, Inc., B1 Pump AssemblyD7043 104temp

34、erature sensor to be a useful diagnostic tool. If used, it shall besuitable for 13.8-MPa duty and should be placed in the high pressure linebetween the pump and the relief valve (Item 18, Fig. 1).6.1.8 Heat Exchanger, (Item 10, Fig. 1). The heat exchangershould be of adequate size and design to remo

35、ve the excessheat from the test system when using the available coolantsupply.NOTE 4It is suggested that a shell-and-tube-type heat exchanger, ifused, should be connected in reverse (the hydraulic fluid is passed throughthe tubes and not around them) so that the interior of the heat exchangercan be

36、effectively cleaned between tests.6.1.9 Pressure Indicator, (Item 6, Fig. 1) to measure pumpdischarge pressure shall have an accuracy of at least 60.3 MPaat 13.8 MPa. The gauge shall be suitable for 13.8-MPa duty.6.1.9.1 The pressure indicator should be snubbed (Item 7,Fig. 1) to prevent damage from

37、 pulsations or sudden fluctua-tions of system pressure.6.1.10 Filter Unit (Item 9, Fig. 1), 3-m (minimum Beta 3ratio of 100) replaceable fiberglass element with housing. Twonew filter elements are required for each test.6.1.10.1 The filter housing shall be non-bypassing and shallbe provided with dua

38、l pressure gauges (Item 13, Fig. 1)oranother suitable indicator to monitor pressure across the filterto warn of impending collapse of the element.6.1.10.2 If dual pressure gauges are used to monitor filterpressure, the rated collapse pressure of the filter element shouldbe known. The collapse pressu

39、re should be within the range ofthe gage.6.1.11 Flow Measuring Device, (Item 12, Fig. 1) with anaccuracy of at least 60.4 L/min.6.1.12 While not required, it is suggested that low-level,high-pressure, high-temperature, and low-flow safety switchesbe incorporated into the system.6.1.13 A check should

40、 be made to ensure that the flush andtest fluid are not incompatible with hoses, seals, or any othermaterials in the system.NOTE 5The use of galvanized iron, aluminum, zinc, and cadmiumshould be avoided because of their high potential for corrosion in thepresence of many non-petroleum hydraulic flui

41、ds.6.1.14 Flexible Motor Coupling, (Item 4, Fig. 1).6.2 The various components of the test system shall beplaced in the system as indicated in Fig. 1.6.2.1 The test system shall be arranged and provided withnecessary drain valves so that complete draining is possiblewith no fluid trap areas.6.2.2 Go

42、od hydraulics piping practices should be used whenconstructing the test system to avoid air ingestment points andflow restrictions.6.2.3 The pump should be mounted so that its internalsurfaces can easily be inspected and cleaned, alignment can bechecked, and the operator has comfortable access when

43、torqu-ing the head.6.2.4 The reservoir shall be located above the pump so thatthe fluid level in the reservoir will be between 61 and 66 cmabove the center line of the pump when the test system is fullycharged with 19 L of test fluid (Dimension A, Fig. 1).6.2.4.1 The reservoir should be mounted so t

44、hat it can becleaned and filled with ease and the contents may be readilyinspected by removal of the reservoir lid.6.2.5 The inlet line (from the reservoir to the pump intake)shall have an internal diameter of at least 25 mm and shall havea straight horizontal run of at least 15 cm to where it conne

45、ctsto the pump inlet port (Dimension B, Fig. 1). If a hose is used,it shall be rated for vacuum service. The B1 pump uses dualinlet hoses with an internal diameter of 22 mm.NOTE 6Some users have found the addition of a compound pressuregage near the pump inlet port to be a useful diagnostic tool (It

46、em 17, Fig.1). However, exercise care to ensure that any ports added to the inlet linedo not become air ingestment points.NOTE 7The use of a solenoid valve, finger screen or other devicewhich restricts pump inlet flow is discouraged. Inlet restrictions adverselyaffect pump performance.NOTE 8When tub

47、ing is used for the pump inlet line, some users preferto use a radius bend instead of an elbow near the pump inlet. If used, thestraight run described in 6.2.5 shall be measured between the end of thebend and the pump inlet port. For optimal flow properties with 25 mmtubing, a 100-mm (4-in.) bend ra

48、dius is recommended.6.2.6 The high pressure discharge line (from the pump to thepressure control valve) shall be rated for 14-MPa (2000-psi)duty and have a minimum internal diameter of 15 mm. The B1pump uses dual discharge hoses with an internal diameter of10.4 mm.6.2.7 The fluid return line and fit

49、tings (from the pressurecontrol valve to the filter, flow counter, heat exchanger, andreservoir) shall be rated for 3-MPa duty and have a minimuminternal diameter of 15 mm.NOTE 9Some users find the addition of a shut off valve on the returnline (Item 16, Fig. 1) to be a useful addition to the piping since it allowsfilter changes and other system maintenance to be performed withoutdraining the reservoir.6.2.7.1 (WarningIf a shut-off valve is installed in thefluid return line, the user shall take procedura