ASTM D7043-2017 red 1875 Standard Test Method for Indicating Wear Characteristics of Non-Petroleum and Petroleum Hydraulic Fluids in a Constant Volume Vane Pump《定容式叶轮泵中非石油和石油液压液磨损特.pdf

《ASTM D7043-2017 red 1875 Standard Test Method for Indicating Wear Characteristics of Non-Petroleum and Petroleum Hydraulic Fluids in a Constant Volume Vane Pump《定容式叶轮泵中非石油和石油液压液磨损特.pdf》由会员分享，可在线阅读，更多相关《ASTM D7043-2017 red 1875 Standard Test Method for Indicating Wear Characteristics of Non-Petroleum and Petroleum Hydraulic Fluids in a Constant Volume Vane Pump《定容式叶轮泵中非石油和石油液压液磨损特.pdf（15页珍藏版）》请在麦多课文档分享上搜索。

1、Designation: D7043 12D7043 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

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

3、operated at 1200 rmin and 13.8 MPa.1.2 The values stated in SI units are to be regarded as standard. No other units of measurement are included in this standard.1.2.1 ExceptionThere are no SI equivalents for the inch fasteners and inch O-rings that are used in the apparatus in this testmethod.1.2.2

4、ExceptionIn some cases English pressure values are given in parentheses as a safety measure.1.3 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibilityof the user of this standard to establish appropriate safety and health pract

5、ices and determine the applicability of regulatorylimitations prior to use.1.4 This international standard was developed in accordance with internationally recognized principles on standardizationestablished in the Decision on Principles for the Development of International Standards, Guides and Rec

6、ommendations issuedby the World Trade Organization Technical Barriers to Trade (TBT) Committee.2. Referenced Documents2.1 ASTM Standards:2D2882 Test Method for Indicating Wear Characteristics of Petroleum and Non-Petroleum Hydraulic Fluids in Constant VolumeVane Pump (Withdrawn 2003)3D6300 Practice

7、for Determination of Precision and Bias Data for Use in Test Methods for Petroleum Products and LubricantsE177 Practice for Use of the Terms Precision and Bias in ASTM Test MethodsE691 Practice for Conducting an Interlaboratory Study to Determine the Precision of a Test Method3. Terminology3.1 Defin

8、itions of Terms Specific to This Standard:3.1.1 flushing, vprocess of cleaning the test system before testing to prevent cross-contamination.3.1.2 torquing, vprocess of tightening the pump head bolts to achieve a uniform clamping force.4. Summary of Test Method4.1 An amount of 18.9 L 6 0.5 L of a hy

9、draulic fluid are circulated through a rotary vane pump system for 100 h at a pumpspeed of 1200 rmin 6 60 rmin and a pump outlet pressure of 13.8 MPa 6 0.3 MPa (2000 psi 6 40 psi). Fluid temperature atthe pump inlet is 66 C 6 3 C for all water glycols, emulsions, and other water containing fluids an

10、d for petroleum and syntheticfluids of ISO Grade 46 or lighter. A temperature of 80 C 6 3 C is used for all other synthetic and petroleum fluids.4.2 The result obtained is the total mass loss from the cam ring and the twelve vanes during the test. Other reported values areinitial flow rate and final

11、 flow rate.1 This test method is under the jurisdiction ofASTM Committee D02 on Petroleum Products, Liquid Fuels, and Lubricants and is the direct responsibility of SubcommitteeD02.N0 on Hydraulic Fluids.Current edition approved June 1, 2012July 1, 2017. Published October 2012July 2017. Originally a

12、pproved in 2004. Last previous edition approved in 20102012 asD7043D7043 12.10. DOI: 10.1520/D7043-12.10.1520/D7043-17.2 For referencedASTM standards, visit theASTM website, www.astm.org, or contactASTM Customer Service at serviceastm.org. For Annual Book of ASTM Standardsvolume information, refer t

13、o the standards Document Summary page on the ASTM website.3 The last approved version of this historical standard is referenced on www.astm.org.This document is not an ASTM standard and is intended only to provide the user of an ASTM standard an indication of what changes have been made to the previ

14、ous version. Becauseit may not be technically possible to adequately depict all changes accurately, ASTM recommends that users consult prior editions as appropriate. In all cases only the current versionof the standard as published by ASTM is to be considered the official document.*A Summary of Chan

15、ges section appears at the end of this standardCopyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United States14.3 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 cha

16、racteristics of non-petroleum and petroleum hydraulic fluids operating in aconstant volume vane pump. Excessive wear in vane pumps could lead to malfunction of hydraulic systems in critical applications.6. Apparatus6.1 The basic system consists of the following (see Fig. 1):6.1.1 AC Motor, 1200 rmin

17、, or other suitable drive, with 11 kw11 kW (15 hp) as suggested minimum power requirement (Item5, Fig. 1). The motor must have right hand rotation (counterclockwise rotation as viewed from the shaft end).6.1.2 Test Stand Base, with appropriate, rigid mounting for the motor, pump, reservoir, and othe

18、r components.6.1.3 Rotary Vane Pump, replaceable cartridge type. AVickers4 V104C or V105C or Conestoga USA B1 housing is used alongwith internal components from Conestoga USA, Inc.5 The assembly should produce 28.428.4 L L/min min flow at 12001200 rr/min min with ISO Grade 32 fluid at 49C,49 C, at 6

19、.9 MPa 6.9 MPa (Item 3, Fig. 1; Fig. 2; Fig. 3). (WarningEaton-Vickerstest pump is rated at 6.9 MPa 6.9 MPa (1000 psi) but is being operated at 13.8 MPa (2000 psi).Aprotective shield around the pumpis recommended.)NOTE 1This test method has been written for the use of Conestoga USA Inc. internals al

20、ong with an Eaton-Vickers or Conestoga USA housing andhead. If components from other manufacturers are used, refer to Test Method D288200 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 vanes, and an ali

21、gnment pin.6.1.3.2 The individual cartridge parts are purchased separately. Conestoga USA, Inc. part numbers for these items are: cam ringNo. 2882-5, alignment pin No. 2882-10, rotor No. 2882-1C, bronze bushings No. 2882-4C and 2882-4E, and vane kit (12 vanes)No. 2882-V12.6.1.3.3 There are to be no

22、modifications to the pump housing such as plugging the drain hole in the pump body or drilling andtapping 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 removable baffle and a close fitting lid, all of stainless steel constru

23、ction. Thereservoir can be square or rectangular (with a flat bottom) or cylindrical (with a spherical or cone shaped bottom) and must bedesigned so as to avoid air entrainment in the fluid.NOTE 2A suitable reservoir design is presented in Test Method D288200. 00.6.1.4.2 To promote deaeration and th

24、ermal mixing of the fluid, the baffle shall be designed so that returning fluid will followan indirect path from the return port to the outlet port.6.1.4.3 To avoid air entrainment, the reservoir shall be designed so that the return line enters well below the fluid level, fluidflow does not cascade

25、over the baffle, and there will be a minimum of 15 cm of fluid depth above the pump inlet line.6.1.4.4 Fluid ports may be added as required by the user for the installation of a low level switch, reservoir temperature sensor,bottom drain, and so forth.6.1.4.5 If the reservoir is positioned so that t

26、he contents cannot be visually checked for aeration by removing the lid, a fluid-tightglass viewing port may be located in the side of the reservoir.6.1.5 Outlet Pressure Control Valve, Eaton-Vickers pressure relief valve (CT-06-C/3.4 to 13.8 MPa) with either manual orremote control (Item 8, Fig. 1)

27、.66.1.6 Temperature Control Device, suitable for controlling coolant 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 an accuracy of 61 C and shall have an appropriate sensor to monitorpump inlet

28、temperature.6.1.7.1 To prevent a flow restriction near the pump inlet port, the temperature probe shall have a diameter of not more than 6mm.6.1.7.2 The test fluid temperature shall be measured within 10.2 cm of the pump inlet (Dimension C, Fig. 1). The sensing probeshall be inserted into the midpoi

29、nt of flow.NOTE 3Some users have found the addition of a pump outlet temperature sensor to be a useful diagnostic tool. If used, it shall be suitable for 13.8 MPaduty and should be placed in the high pressure line between the pump and the relief valve (Item 18, Fig. 1).4 Previously available, this a

30、pparatus was made obsolete in 2000 byVickers, which is part of Eaton Hydraulics Group USA14615 Lone Oak Road Eden Prairie, MN 55344.If you are aware of alternative suppliers, please provide this information toASTM International Headquarters. Your comments will receive careful consideration at a meet

31、ingof the responsible technical committee,1 which you may attend.5 The sole source of supply of the apparatus known to the committee at this time is Conestoga USA Inc., P.O. Box 3052, Pottstown, PA 19464. If you are aware ofalternative suppliers, please provide this information to ASTM International

32、 Headquarters. Your comments will receive careful consideration at a meeting of the responsibletechnical committee,1 which you may attend.6 Request Vickers publication I-3369-S for the relief valve service data. See http:/ 172Item Description Required?1. Reservoir2. Inlet temperature sensor3. Pump4.

33、 Flexible coupling5. Motor6. High pressure 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.

34、Outlet temperature sensor Not required19. 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 1736.1.8 Heat Exchanger, (Item 10, Fig. 1). The heat exchanger should be of adequate size and design to rem

35、ove the excess heatfrom the test system when using the available coolant supply.NOTE 4It is suggested that a shell-and-tube-type heat exchanger, if used, should be connected in reverse (the hydraulic fluid is passed through thetubes and not around them) so that the interior of the heat exchanger can

36、 be effectively cleaned between tests.6.1.9 Pressure Indicator, (Item 6, Fig. 1) to measure pump discharge pressure shall have an accuracy of at least 60.3 MPa at13.8 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 damag

37、e from pulsations or sudden fluctuations ofsystem pressure.6.1.10 Filter Unit (Item 9, Fig. 1), 3 m (minimum Beta 3 ratio of 100) replaceable fiberglass element with housing. Two newfilter elements are required for each test.6.1.10.1 The filter housing shall be non-bypassing and shall be provided wi

38、th dual pressure gauges (Item 13, Fig. 1) or anothersuitable indicator to monitor pressure across the filter to warn of impending collapse of the element.6.1.10.2 If dual pressure gauges are used to monitor filter pressure, the rated collapse pressure of the filter element should beknown. The collap

39、se pressure should be within the range of the gage.6.1.11 Flow Measuring Device, (Item 12, Fig. 1) with an accuracy of at least 60.4 Lmin.6.1.12 While not required, it is suggested that low-level, high-pressure, high-temperature, and low-flow safety switches beincorporated into the system.Descriptio

40、n of ItemsItem Number Name Amount Description1 Head Bolt 8 38-16 1-14-in. hex head cap screw, Grade 82 Head Bearing 1 No. 6200, open type3 Pump Head 1 Vickers 240644 Head PackingA 1 235 square cut O-ring5 Outer Bushing 1 Conestoga 2882-4E6 Alignment Pin 1 Conestoga 2882-107 Cam RingB 1 Conestoga 288

41、2-58 RotorB 1 Conestoga 2882-1C9 VaneB 12 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 3AM12013 Shaft Bearing 1 #6204, open type14 Seal Retainer 1 Vickers 18507815 O-RingA 1 223 O-ring16 Shaft SealA 1

42、 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 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 6 38-16 78 socket

43、 head cap screwA Specify compound.B Specify size.FIG. 2 Pump ComponentsD7043 1746.1.13 A check should be made to ensure that the flush and test fluid are not incompatible with hoses, seals, or any othermaterials in the system.NOTE 5The use of galvanized iron, aluminum, zinc, and cadmium should be av

44、oided because of their high potential for corrosion in the presenceof 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 be placed in the system as indicated in Fig. 1.6.2.1 The test system shall be arranged and pr

45、ovided with necessary drain valves so that complete draining is possible with nofluid trap areas.6.2.2 Good hydraulics piping practices should be used when constructing the test system to avoid air ingestment points and flowrestrictions.6.2.3 The pump should be mounted so that its internal surfaces

46、can easily be inspected and cleaned, alignment can be checked,and the operator has comfortable access when torquing the head.6.2.4 The reservoir shall be located above the pump so that the fluid level in the reservoir will be between 61 cm and 66 cmabove the center line of the pump when the test sys

47、tem is fully charged with 19 L of test fluid (Dimension A, Fig. 1).6.2.4.1 The reservoir should be mounted so that it can be cleaned and filled with ease and the contents may be readily inspectedby removal of the reservoir lid.6.2.5 The inlet line (from the reservoir to the pump intake) shall have a

48、n internal diameter of at least 25 mm and shall have astraight horizontal run of at least 15 cm to where it connects to the pump inlet port (Dimension B, Fig. 1). If a hose is used, it shallbe rated for vacuum service. The B1 pump uses dual inlet hoses with an internal diameter of 22 mm.NOTE 6Some u

49、sers have found the addition of a compound pressure gage 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 line do not become air ingestment points.NOTE 7The use of a solenoid valve, finger screen or other device which restricts pump inlet flow is discouraged. Inlet restrictions adversely affectpump performance.NOTE 8When tubing is used for the pump inlet line, some users prefer to use a ra