ASTM D7043-17 Standard Test Method for Indicating Wear Characteristics of Non-Petroleum and Petroleum Hydraulic Fluids in a Constant Volume Vane Pump.pdf

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1、Designation: D7043 17Standard 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 rmin 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

4、some 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 dete

5、rmine the applica-bility of regulatory limitations prior to use.1.4 This international standard was developed in accor-dance with internationally recognized principles on standard-ization established in the Decision on Principles for theDevelopment of International Standards, Guides and Recom-mendat

6、ions issued by the World Trade Organization TechnicalBarriers to Trade (TBT) Committee.2. Referenced Documents2.1 ASTM Standards:2D2882 Test Method for Indicating Wear Characteristics ofPetroleum and Non-Petroleum Hydraulic Fluids in Con-stant Volume Vane Pump (Withdrawn 2003)3D6300 Practice for Det

7、ermination of Precision and BiasData for Use in Test Methods for Petroleum Products andLubricantsE177 Practice for Use of the Terms Precision and Bias inASTM Test MethodsE691 Practice for Conducting an Interlaboratory Study toDetermine the Precision of a Test Method3. Terminology3.1 Definitions of T

8、erms Specific to This Standard:3.1.1 flushing, vprocess of cleaning the test system beforetesting to prevent cross-contamination.3.1.2 torquing, vprocess of tightening the pump head boltsto achieve a uniform clamping force.4. Summary of Test Method4.1 An amount of 18.9 L 6 0.5 L of a hydraulic fluid

9、 arecirculated through a rotary vane pump system for 100 h at apump speed of 1200 rmin 6 60 rmin and a pump outletpressure of 13.8 MPa 6 0.3 MPa (2000 psi 6 40 psi). Fluidtemperature at the pump inlet is 66 C 6 3 C for all waterglycols, emulsions, and other water containing fluids and forpetroleum a

10、nd synthetic fluids of ISO Grade 46 or lighter. Atemperature of 80 C 6 3 C is used for all other synthetic andpetroleum fluids.4.2 The 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

11、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 character-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 hydraul

12、ic systems incritical applications.6. Apparatus6.1 The basic system consists of the following (see Fig. 1):6.1.1 AC Motor, 1200 rmin, or other suitable drive, with11 kW (15 hp) as suggested minimum power requirement1This test method is under the jurisdiction of ASTM Committee D02 onPetroleum Product

13、s, Liquid Fuels, and Lubricants and is the direct responsibility ofSubcommittee D02.N0 on Hydraulic Fluids.Current edition approved July 1, 2017. Published July 2017. Originally approvedin 2004. Last previous edition approved in 2012 as D7043 12. DOI: 10.1520/D7043-17.2For referenced ASTM standards,

14、 visit the ASTM website, www.astm.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.3The last approved version of this historical standard is referenced onwww.astm.org.*A Summa

15、ry of Changes section appears at the end of this standardCopyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United StatesThis international standard was developed in accordance with internationally recognized principles on standardization established

16、in the Decision on Principles for theDevelopment of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.1Item Description Required?1. Reservoir2. Inlet temperature sensor3. Pump4. Flexible coupling5. Motor6. High pres

17、sure gauge7. Snubber valve8. 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 required

18、19. Case drain for B1 pumpA. 61 to 66 cm, vertical RequiredB. 15.2 cm, minimum horizontal RequiredC. 10.2 cm, maximum RequiredFIG. 1 System SchematicD7043 172(Item 5, Fig. 1). The motor must have right hand rotation(counterclockwise rotation as viewed from the shaft end).6.1.2 Test Stand Base, with

19、appropriate, rigid mounting forthe motor, pump, reservoir, and other components.6.1.3 Rotary Vane Pump, replaceable cartridge type. AVickers4V104C or V105C or Conestoga USA B1 housing isused along with internal components from Conestoga USA,Inc.5The assembly should produce 28.4 Lmin flow at1200 rmin

20、 with ISO Grade 32 fluid at 49 C, at 6.9 MPa (Item3, Fig. 1; Fig. 2; Fig. 3). (WarningEaton-Vickers test pumpis rated at 6.9 MPa (1000 psi) but is being operated at 13.8MPa (2000 psi). A protective shield around the pump isrecommended.)NOTE 1This test method has been written for the use of Conestoga

21、USA Inc. internals along with an Eaton-Vickers or Conestoga USAhousing and head. If components from other manufacturers are used, referto Test Method D2882 00 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

22、vanes, and an alignmentpin.6.1.3.2 The individual cartridge 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-V12.4Previously

23、 available, this apparatus was made obsolete in 2000 by Vickers,which is part of Eaton Hydraulics Group 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 cons

24、id-eration at a meeting of the responsible technical committee,1which you may attend.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

25、ASTM InternationalHeadquarters. Your comments will receive careful consideration at a meeting of theresponsible technical committee,1which you may attend.Description of ItemsItem Number Name Amount Description1 Head Bolt 838-161-14-in. hex head cap screw, Grade 82 Head Bearing 1 No. 6200, open type3

26、 Pump Head 1 Vickers 240644 Head PackingA1 235 square 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

27、 Retaining Ring 1 20-mm steel retaining ring 3AM12013 Shaft Bearing 1 #6204, open type14 Seal Retainer 1 Vickers 18507815 O-RingA1 223 O-ring16 Shaft SealA1 double lip with garter spring .875 1.500 .312 rubber clad17 Shaft 1 Conestoga 2882-2A18 Key 1 Conestoga 2882-20A or Vickers 161219a Foot Mount

28、1 Vickers 18823419b Flange Mount 1 Vickers 18823320 Gasket 1 Conestoga 2882-27 or Vickers 2546 not used with Foot Mount (item 19a)21 Screw 638-16 78 socket head cap screwASpecify compound.BSpecify size.FIG. 2 Pump ComponentsD7043 1736.1.3.3 There are to be no modifications to the pumphousing such as

29、 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 recta

30、ngular (with a flat bottom)or cylindrical (with a spherical or cone shaped bottom) andmust be designed so as to avoid air entrainment in the fluid.NOTE 2A suitable reservoir design is presented in Test MethodD2882 00.6.1.4.2 To promote deaeration and thermal mixing of thefluid, the baffle shall be d

31、esigned 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 reservoir 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

32、 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, 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 b

33、y removing the lid, afluid-tight glass viewing port may be located in the side of thereservoir.6.1.5 Outlet Pressure Control Valve, Eaton-Vickers 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 contro

34、llingcoolant flow to the heat exchanger to maintain test fluid at thespecified temperature (Item 11, Fig. 1).6.1.7 Temperature Indicator, (Item 2, Fig. 1) shall have anaccuracy of 61 C and shall have an appropriate sensor tomonitor pump inlet temperature.6.1.7.1 To prevent a flow restriction near th

35、e 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 within10.2 cm of the pump inlet (Dimension C, Fig. 1). The sensingprobe shall be inserted into the midpoint of flow.6Request Vickers publication I-3369-S for the re

36、lief valve service data. Seehttp:/ 3 Conestoga USA, Inc., B1 Pump AssemblyD7043 174NOTE 3Some users have found the addition of a pump outlettemperature 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

37、 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 remove the excessheat from the test system when using the available coolantsupply.NOTE 4It is suggested that a shell-and-tube-type heat exchanger, ifused, shoul

38、d be connected in reverse (the hydraulic fluid is passed throughthe tubes and not around them) so that the interior of the heat exchangercan be 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

39、 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 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

40、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 dual 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 I

41、f dual pressure gauges are used to monitor filterpressure, the rated collapse pressure of the filter element shouldbe known. The collapse pressure should be within the range ofthe gage.6.1.11 Flow Measuring Device, (Item 12, Fig. 1) with anaccuracy of at least 60.4 Lmin.6.1.12 While not required, it

42、 is suggested that low-level,high-pressure, high-temperature, and low-flow safety switchesbe incorporated into the system.6.1.13 A check should 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,

43、 aluminum, zinc, and cadmiumshould be avoided because of their high potential for corrosion in thepresence of many non-petroleum hydraulic fluids.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 T

44、he test system shall be arranged and provided withnecessary drain valves so that complete draining is possiblewith no fluid trap areas.6.2.2 Good hydraulics piping practices should be used whenconstructing the test system to avoid air ingestment points andflow restrictions.6.2.3 The pump should be m

45、ounted so that its internalsurfaces can easily be inspected and cleaned, alignment can bechecked, and the operator has comfortable access when 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 cm and 66 cmabove the cente

46、r 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 that 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 reservoi

47、r 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 connectsto 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

48、 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 (Item 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 valv

49、e, finger screen or other devicewhich restricts pump inlet flow is discouraged. Inlet restrictions adverselyaffect pump performance.NOTE 8When tubing 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 radius is recommended.6.2.6 The high pressure dis