ASTM D7043-2012 red 9061 Standard Test Method for Indicating Wear Characteristics of Non-Petroleum and 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.pdf

《ASTM D7043-2012 red 9061 Standard Test Method for Indicating Wear Characteristics of Non-Petroleum and 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.pdf》由会员分享，可在线阅读，更多相关《ASTM D7043-2012 red 9061 Standard Test Method for Indicating Wear Characteristics of Non-Petroleum and 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.pdf（14页珍藏版）》请在麦多课文档分享上搜索。

1、Designation:D704310 Designation: D7043 12Standard 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

2、 oforiginal 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 tes

3、t procedure operated at 1200 rpm 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 testme

4、thod.1.2.2 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 h

5、ealth practices and determine the applicability of regulatorylimitations prior to use.2. Referenced Documents2.1 ASTM Standards:2D2882 Test Method for Indicating Wear Characteristics of Petroleum and Non-Petroleum Hydraulic Fluids in Constant VolumeVane PumpD6300 Practice for Determination of Precis

6、ion and Bias Data for Use in Test Methods for Petroleum Products and LubricantsE691 Practice for Conducting an Interlaboratory Study to Determine 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 before

7、 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 6 0.5 L of a hydraulic fluid are circulated through a rotary vane pump system for 100 h at a pump speedof 1200 6 60 r/

8、min and a pump outlet pressure of 13.8 6 0.3 MPa (2000 6 40 psi). Fluid temperature at the pump inlet is 666 3C for all water glycols, emulsions, and other water containing fluids and for petroleum and synthetic fluids of ISO Grade 46or lighter. A temperature of 80 6 3C is used for all other synthet

9、ic 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 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

10、 an indicator of the wear characteristics 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.

11、 1):1This test method is under the jurisdiction of ASTM Committee D02 on Petroleum Products and Lubricants and is the direct responsibility of Subcommittee D02.N0.07on Lubricating Properties.Current edition approved MayJune 1, 2010.2012. Published September 2010.October 2012. Originally approved in

12、2004. Last previous edition approved in 20042010 asD704304a.D704310. DOI: 10.1520/D7043-102.2For referencedASTM standards, visit theASTM website, www.astm.org, or contactASTM Customer Service at serviceastm.org. For Annual Book of ASTM Standardsvolume information, refer to the standards Document Sum

13、mary page on the ASTM website.1This 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 previous version. Becauseit may not be technically possible to adequately depict all changes accurately, ASTM recommen

14、ds 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 Changes section appears at the end of this standard.Copyright ASTM International, 100 Barr Harbor Drive, PO Box C700,

15、 West Conshohocken, PA 19428-2959, United States.Item Description Required?1. Reservoir2. Inlet temperature sensor3. Pump4. Flexible coupling5. Motor6. High pressure gauge7. Snubber valve8. Relief valve9. Filter10. Heat exchanger11. Temperature control valve12. Flow meter13. Low pressure gauge14. Fl

16、uid 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 pumpA. 61 to 66 cm, vertical RequiredB. 15.2 cm, minimum horizontal RequiredC. 10.2 cm, maximum RequiredFIG. 1 System

17、 SchematicD7043 1226.1.1 AC Motor, 1200-rpm, or other suitable drive, with 11 kw (15 hp) as suggested minimum power requirement (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 appropriate, rigid mounting fo

18、r the motor, pump, reservoir, and other components.6.1.3 Rotary Vane Pump, replaceable cartridge type. AVickers3V104C or V105C or Conestoga USA B1 housing is used alongwith internal components from Conestoga USA, Inc.4The assembly should produce 28.4 L/min flow at 1200 r/min with ISO Grade32 fluid a

19、t 49C, at 6.9 MPa (Item 3, Fig. 1; Fig. 2; Fig. 3). (WarningEaton-Vickers test pump is rated at 6.9 MPa (1000 psi)but is being operated at 13.8 MPa (2000 psi). A protective shield around the pump is recommended.)NOTE 1This test method has been written for the use of Conestoga USA Inc. internals alon

20、g with an Eaton-Vickers or Conestoga USA housing andhead. If components from other manufacturers are used, refer to 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 alignmen

21、t pin.3Previously available, this apparatus 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 rece

22、ive careful consideration at a meetingof the responsible technical committee, which you may attend.4The 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

23、information to ASTM International Headquarters. Your comments will receive careful consideration at a meeting of the responsibletechnical committee, which 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 N

24、o. 6200, open type3 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

25、 1 Vickers 18823512 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 3 1.500 3 .312 rubber clad17 Shaft 1 Conestoga 2882-2A18 Key 1 Conestoga 2882-20A or Vick

26、ers 161219a Foot Mount 1 Vickers 18823419b Flange Mount 1 Vickers 18823320 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 1236.1.3.2 The individual cartridge parts are pu

27、rchased 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 modifications to the pump housing such as plugging the d

28、rain 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 construction. Thereservoir can be square or rectangular (with a

29、 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 D288200.6.1.4.2 To promote deaeration and thermal mixing of the fluid, the baffle shall be designed so t

30、hat 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 over the baffle, and there will be a minimum of 15 cm of flu

31、id 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 the contents cannot be visually checked for aeration by remov

32、ing 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).56.1.6 Temperature Control Device, suitable for controlling

33、 coolant flow to the heat exchanger to maintain test fluid at thespecified temperature (Item 11, Fig. 1).5Request Vickers publication I-3369-S for the relief valve service data. See http:/ 3 Conestoga USA, Inc., B1 Pump AssemblyD7043 1246.1.7 Temperature Indicator, (Item 2, Fig. 1) shall have an acc

34、uracy of 61C and shall have an appropriate sensor to monitorpump inlet 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 (D

35、imension C, Fig. 1). The sensing probeshall be inserted into the midpoint 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 for13.8-MPa duty and should be placed in the high pressure line between the pum

36、p and the relief valve (Item 18, Fig. 1).6.1.8 Heat Exchanger, (Item 10, Fig. 1). The heat exchanger should be of adequate size and design to remove 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, s

37、hould be connected in reverse (the hydraulic fluid is passed through thetubes and not around them) so that the interior of the heat exchanger can 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

38、 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 damage 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 el

39、ement 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 with 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

40、.1.10.2 If dual pressure gauges are used to monitor filter pressure, the rated collapse pressure of the filter element should beknown. The collapse 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 L/min.6.1.12 While not

41、 required, it is suggested that low-level, high-pressure, high-temperature, and low-flow safety switches beincorporated into the system.6.1.13 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 g

42、alvanized iron, aluminum, zinc, and cadmium should be avoided 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

43、in Fig. 1.6.2.1 The test system shall be arranged and provided 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 T

44、he pump should be mounted so that its internal surfaces 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 and 66

45、cm abovethe center line of the pump when the test system 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

46、 (from the reservoir to the pump intake) shall have an 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

47、hoses with an internal diameter of 22 mm.NOTE 6Some users 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 7Th

48、e 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 radius bend instead of an elbow near the pump inlet. If used, the

49、straight run described in 6.2.5 shall be measured between the end of the bend and the pump inlet port. For optimal flow properties with 25 mm tubing,a 100-mm (4-in.) bend radius is recommended.6.2.6 The high pressure discharge line (from the pump to the pressure control valve) shall be rated for 14-MPa (2000-psi) dutyand have a minimum internal diameter of 15 mm. The B1 pump uses dual discharge hoses with an internal diameter of 10.4 mm.6.2.7 The fluid return line and fittings (from the pressure control