Continental Hydraulics HPV-6, HPV-10, HPV-15, HPV-20, HPV-29 Service Manual

CAUTION – Before performing any service
operation on any pump, be sure that all pressure has been relieved from the system.
CAUTION – Before performing any service operation on any pump, disconnect or lock off power supply.
CAUTION – Before starting any pump, be sure that any resulting machine function will not endanger persons or equipment.
PRODUCT IDENTIFICATION
Each HPV Piston Pump has a Model Code stamped on its escutcheon plate. See Figure 1 for the location of the Model Code.
Date
Code
Model
Code
Figure 1
This Service Booklet applies to products with Model Codes like the sample in Figure 2.
Basic Pump Rotation
Seal Type Ports
HPV - 6B35-RF-O-1R
Figure 2
SERVICE MANUAL
HPV Axial Piston Pumps
“B” Design Series
GENERAL SPECIFICATIONS
MOUNTING
Any unrestricted mounting position acceptable. Horizontal mounting preferred. The mounting hub and two-bolt mounting flange conform to SAE mounting standards.
Continental Hydraulics does not recommend direct rigid connection of piston pumps to the Prime Mover. Use of a flexible coupling, a coupling that allows for minor misalignment is recommended.
If the shaft connection to the Prime Mover is rigid, the mounting face diametric concentricity and squareness must be within .001 inch (0.03 mm) T.I.R. for a flange mounted pump.
The HPV Piston Pump is designed for in-line drive. Angle drive creates side loads on the shaft, and is not acceptable.
SHAFT INFORMATION Splined:
The coupling interface must be lubricated. Continental Hydraulics recommends lithium molydisulfate, or similar grease. The female coupling should be hardened to 27-45 Rc, and must conform to ANSI B92.1 Class 5 Fillet or Flat Root Side Fit.
Keyed:
High strength heat treated keys must be used. Replacement keys must be hardened to 27-34 Rc. Key corners must be chamfered .030 - .040 inch (.75
- 1.0 mm) at 45° to clear radii in the keyway.
PLUMBING
Connect inlet and outlet lines to the pump’s cover. HPV fluid connections are SAE straight thread, SAE flange or BSPP.
MODEL REAR PORT SIDE PORT
HPV-6 SAE-12 or 3/4” BSPP SAE-16 or 1” BSPP HPV-10 SAE-20 or 1-1/4” BSPP SAE-20 or 1-1/4” BSPP HPV-15 SAE-20 or 1-1/4” BSPP SAE-20 or 1-1/4” BSPP HPV-20 SAE-20 or 1-1/4” BSPP SAE1-1/4” Flange* HPV-29 SAE-20 or 1-1/4” BSPP SAE1-1/2” Flange**
* Per Code 62 ** Per Code 61
Maximum case pressure is 10 psi (0.70 bar). Case pressure must never exceed inlet pressure by more than 15 psi (1.0 bar). To prevent fluid drain-down from the pump when idle, make certain that case drain plumbing passes above the highest point of the pump before entering the reservoir. Or, install a 5 psi (.3 bar) case pressure check valve to assure that the pump is always filled with hydraulic fluid.
The case drain line must be big enough to prevent back pressure in excess of 10 psi (0.70 bar).
Form No. R92.00 Rev. 10/03
1
PLUMBING (continued...) Hydraulic fluid from the case drain line should be
returned to the reservoir below the fluid level, and as far from the supply intake as possible. All fluid lines (whether pipe, tubing or hose) must be of adequate size and strength to assure free flow through the pump. Do not tee return lines together.
SYSTEM RELIEF VALVES
Although HPV series pumps have a very fast off­stroke compensator response, fast acting relief valves are recommended in all cases for safety. They also help reduce transient pressure spikes.
RECOMMENDED FLUID
Note: The following fluid recommendations
and specifications apply to HPV series pumps only. Assure that all other components in the hydraulic system have compatible requirements.
Petroleum-based, and most phosphate esters. Fluids should be designated by the manufacturer for use in hydraulic systems. Fluids should be formulated with oxidation inhibitors, anti-rust, anti-foam and deaerating agents. Other fluids may be acceptable, but special O-rings may be required. Nitrile (Buna) seals are standard.
VISCOSITY
Maximum at full power . . . . . . .750 SUS (160 Cst)
Optimum for maximum life . . . .140 SUS (30 Cst)
Minimum at full power . . . . . . . 60 SUS (10 Cst)
VISCOSITY INDEX
90 V.I. minimum. Higher values extend the operating temperature range, but may reduce fluid service life.
Fluid Operating Temperature – Operating temperature should be determined by the viscosity characteristics of the fluid used. Fluid temperature in the reservoir during operation should be kept between 100° F. and 130° F. (38° C. and 54° C.) Because high temperature degrades seals, reduces service life and creates hazards, fluid temperature should not exceed 180° F. (82° C.) at the case drain.
CAUTION – Fluid temperatures in excess of 120° F. (49° C.) can cause serious burns and scalding. Allow fluid to cool before performing any repairs or maintenance.
Fluid Cleanliness – Control particle contamination by changing or cleaning all filter elements periodically BEFORE they become clogged and start to by-pass. Fluid must be cleaned before and continuously during operation to a cleanliness level of ISO 18/16/13 or better. This level of cleanliness can usually be accomplished by use of 10 micron filters. Better fluid cleanliness will significantly extend component life. Since contaminant generation varies with each application, each must be analyzed to determine proper filtration to maintain required cleanliness.
After Extended Shutdowns – Some types of hydraulic fluids become tacky after long periods of non-use. If possible, hand turn the pump several times after extended shutdowns to assure that all components move freely before powering up.
CAUTION – Before hand turning any pump, be sure that any resulting machine function will not endanger persons or equipment.
PREVENTIVE MAINTENANCE
This pump is self-lubricating. Preventive maintenance is limited to keeping the system fluid clean by changing filters regularly. Since filtering needs can vary depending on applications, filters used with this pump should be equipped with indicators that show when changes are needed. Do not operate the pump in a system with clogged or bypassing filters.
Keep all fittings and screws tight. Do not operate this pump at pressures or speeds in excess of stated limits. If the pump does not operate properly, check the Trouble Shooting Section of this manual before attempting to overhaul the pump.
Overhauls are relatively simple, and are covered in the Repair Procedures Section of this manual.
Note: It is especially important to keep suction or inlet piping and fittings tight and in good repair. Air drawn into the system through loose or damaged intake fittings can cause the pump to fail.
START UP PROCEDURE FOR NEW INSTALLATION
1. Read and understand the Service Manual. Identify components and their functions.
2. Visually inspect system
Case Drain
Ports
components and lines for possible damage.
3. Check reservoir for cleanliness. Drain and clean as required.
4. Check reservoir fluid level and fill as required with filtered fluid that
Figure 3
meets or exceeds ISO 18/16/13 cleanliness level. Fill pump through either Case Drain Port (Figure 3).
5. Check drive alignment.
6. Check and activate oil cooler (if included in circuit). Check fluid temperature.
7. Reduce relief valve pressure settings. Make sure accurate pressure readings can be made at appropriate places.
8. If the system includes solenoids, check for proper actuation.
9. Jog electric motor to confirm proper rotation. Jogging the electric motor primes the pump and bleeds air from the system.
10. Start pump drive. Look for leaks, and listen for excessive noise at the pump. If leaks, chattering or other noises are observed, immediately turn the pump off. Corrective actions are covered in the Trouble Shooting Section.
11. Cycle unloaded machine at low pressure, and observe actuation (at low speed, if possible).
12. Increase pressure settings gradually. Check for leaks in all lines, especially in the pump inlet line.
13. Adjust system pressure as needed.
14. Gradually increase system speed to normal operating level. Be alert for trouble as indicated by noise, sound changes, system shocks, leaks, or air bubbles in the reservoir.
2
Form No. R92.00 Rev. 10/03
START UP PROCEDURE (continued...)
15. When the system is running normally, check fluid level and temperature at the reservoir. Repeat these checks periodically. Excessive fluid temperatures will damage the pump. If fluid temperature does not stabilize at 140° F (60° C.) or less, stop the system and take appropriate corrective action.
16. System is operational. Follow appropriate maintenance procedures to assure fluid cleanliness and proper operating temperature.
REPLACEMENT PUMP INSTALLATION
To prevent premature pump failure, make sure that the entire hydraulic circuit is flushed completely clean before installing and operating a replacement pump.
Simply draining the reservoir or relying on the system’s filters is not enough to adequately clean the fluid. Debris trapped in other components or lines may damage the components themselves, or be drawn into the pump. Failure to properly flush the system before installing a replacement pump voids the pump’s warranty.
The following procedures checklist will help you replace a hydraulic pump with confidence that it will provide satisfactory pump life.
1. Determine the cause of the failure (be sure you have found the cause, and not simply a symptom).
2. Eliminate the cause of the failure.
3. Drain the entire circuit, including cylinders, motors, reservoirs, control valves, heat exchangers, and filters.
4. Remove system lines and components. Flush with a compatible solvent, or clean filtered oil to remove contamination that may have entered the system when the pump failed. Be certain that fluid has been flushed from cylinders.
5. Visually inspect components for possible contamination, and for proper operation. Pay special attention to wipers on cylinder rods. Be sure that the rods are free of nicks and scratches.
6. Flush the reservoir using pressurized solvent. Use clean, dry, lint-free cloths to ensure a clean interior. Inspect the filler/breather (if used) and the suction strainer for cleanliness.
7. Install a new filter with a 10 micron or better element, and low Beta ratio. If the machine does not have a filter, install one that meets these specifications.
8. Fill the reservoir with new, FILTERED oil of the recommended type. Be certain to monitor the fluid level, since the entire system (not just the reservoir) must be filled.
9. Re-install all system lines. Visually inspect to make sure they are clean, and free of contamination. Be sure that all inlet fittings are tight and clean.
10. Install the new pump.
11. Follow the start-up procedures given on pages 2 and 3 of this manual.
12. Cycle all cylinders and operate all motors at normal operating speeds for 20 minutes. While operating, observe the reservoir fluid level, since all components will be filling with hydraulic fluid.
13. Replace the filter element, and check the fluid level. Add new, clean, filtered oil if required.
To assure that your replacement pump performs at the same level as the original pump, check daily for proper fluid level, filter condition and leaks. Change fluid at recommended intervals. Good fluid maintenance is especially important when using other than mineral based fluids.
TROUBLESHOOTING GUIDE
Component problems and circuit problems are often interrelated. Apoorly designed circuit may operate with apparent success, but cause a component of the
not the cause of the problem. The following general guide is offered to help you locate and eliminate the cause of problems by studying their effects.
system to fail. The component failure is the effect,
Problem Possible Cause Look For
Noisy Pump Air in fluid Leak in suction line
Leak in shaft seal Low fluid level Turbulent fluid Return lines above fluid level Gas leak from accumulator Excessive pressure drop in the inlet line
from a pressurized reservoir
Cavitation in pump rotating group Fluid too cold, too viscous or too heavy
Shaft speed too high Suction line too small, or collapsed Suction line strainer dirty or too small
Form No. R92.00 Rev. 10/03
Continued on Page 4
3
TROUBLESHOOTING GUIDE
Problem Possible Cause Look For
Noisy Pump Misaligned shaft Faulty installation
Distortion in mounting Axial interference Faulty coupling
Mechanical fault in pump Piston and shoe loose or failed
Bearing failure Incorrect port plate selection or index Eroded or worn parts in
displacement control
Erosion on Air in fluid Refer to above barrel and
Cavitation Refer to above
port plate High wear Excessive loads Reduce speed or pressure setting
in pump
Contaminant particles in fluid Improper filter maintenance
Filter too coarse Dirty fluid introduced to the system Reservoir or breather cap open to
atmosphere
Improper line replacement
Improper fluid Fluid too thick or too thin for operating
temperature range
Fluid breakdown due to age, temperature
or shearing effects Incorrect additives in new fluid Reduced additive effectiveness due to
chemical aging
Improper repair Incorrect parts, procedures, dimensions
or finishes
Unwanted water in fluid Condensation
Faulty breather/strainer Heat exchanger leaking Faulty clean-up practice Water in makeup fluid
Pressure Cogging or erratic load movement Mechanical considerations shocks
Slow acting relief valve Replace with fast acting relief valve Worn relief valve Repair or replace, as needed Worn compensator Repair or replace, as needed Insufficient line capacitance (line volume, Increase line size or length
line stretch, accumulator effects)
Fluid Excessive pump leakage Recheck case drain flow, overheats repair as needed
Fluid too thin, minimum operating viscosity
60 SUS (10Cst) Improper assembly
Faulty relief valve Set too low (compared to load
or compensator) Instability caused by back pressure,
or worn parts
Faulty compensator Set too high (compared to relief)
Worn parts
Faulty heat exchanger Water turned off, or insufficient flow
Ambient water temperature too high Fan clogged, restricted or inoperative Mud or scale buildup Intermittent hydraulic fluid flow through
exchanger
Continued on Page 5
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Form No. R92.00 Rev. 10/03
TROUBLESHOOTING GUIDE (continued)
Problem Possible Cause Look For
Fluid Faulty reservoir Fluid level too low overheats
(continued)
Entrained air in fluid Improper, or no baffles Poor air flow, or ambient air temperature
too high around reservoir
Heat pick up from adjacent equipment
Decrease in Loose compensator adjusting screw Tighten adjusting screw ( No.11 in set pressure Fig. 14, exploded view)
Defective function or relief valves Repair or replace relief valve
Check relief valve setting
Reservoir fluid level too low Replenish fluid
Check drain (below 5% of discharge at
rated pressure)
Deteriorating pump performance Check pump internal components for wear,
repair or replace as needed.
Pressure Pump turning backward Change the rotating direction does not rise
Reservoir fluid level too low Replenish fluid Relief valve or compensator set wrong Readjust and lock Relief valve or compensator defective Repair or replace Clogged suction line Inspect and clean suction strainers
Open gate valve
Deteriorating pump performance Check pump internal components for wear,
repair or replace as needed.
Insufficient Reservoir fluid level too low Replenish fluid flow
Suction line not sealed Tighten fittings Improper pump stroke control adjustment Readjust as required
Repair or replace as required
Deteriorating pump performance Change compensator Worn compensator
PISTON PUMP DISASSEMBLY Precautions
CAUTION – Before performing any service
operation on any pump, be sure that all pressure has been relieved from BOTH SIDES of the system.
CAUTION – Before performing any service operation on any pump, disconnect or lock off power supply.
CAUTION – Do not attempt to remove the Barrel Spring. The Barrel Spring is
assembled under high compression. Any
attempt to remove the Barrel Spring will cause sudden decompression, and may inflict serious personal injury. The Barrel Spring is NOT field serviceable. Should the Barrel Spring require service, the pump must be returned to Continental Hydraulics or an Authorized Repair Center.
1. Please refer to the exploded view (Figure 14 through 17) for proper names and locations of all parts.
Form No. R92.00 Rev. 10/03
2. Pump disassembly for inspection and repair should be undertaken only in the following cases:
Malfunction or leakage due to damage or wear. When troubleshooting procedures contained in this manual do not solve a problem.
3. Disassembly should be done only as far as necessary to replace or repair worn parts.
4. Perform assembly and disassembly in a clean environment.
5. Avoid dropping, damaging or contaminating the machined parts of the pump and compensator.
6. After disassembly, coat the internal parts with a film of clean oil, and protect them from dirt and moisture.
7. Prior to disassembly, measure and record the length of the protruding part of adjusting screws (22) and (28-11) from Figure 14, and if necessary, (18) from Figure 16 or 17. This will simplify resetting the pump after reassembly.
5
HPV REPAIR PROCEDURES
DISASSEMBLY, INSPECTION and REASSEMBLY GENERAL
Disassembly in the field by other than an Authorized Repair Center technician, whether for repair or modification will void warranty.
NOTE: Certain steps in this procedure require special tools, and the application of great force. Care should also be taken
to contain residual oil during disassembly. Before beginning, read this section through to make sure that you are prepared for the job.
General Disassembly Procedure
1. Drain pump body (1) via Case Drain Ports. (Figure 4)
2. Position the pump with Case Drain Ports up.
3. Remove four compensator screws (71) and then remove remove compensator (28) and O­rings (32).
4. Remove four cover retaining screws (46). Loosen two diagonally positioned screws first. Then loosen the remaining two diagonally positioned screws. Remove the screws and carefully separate the cover (2) from the pump body. If the gasket holds the cover in place, tap the cover lightly with a fiber hammer on the side opposite the compensator.
NOTE: The port plate (4) may cling to the cover (2) due to oil film between parts. DO NOT ALLOW THE PLATE TO FALL AND BE DAMAGED.
5. Gently remove the port plate (4) from the barrel (3) face.
6. Place the pump on a work bench with the shaft in a horizontal position. Remove the barrel (3) with piston assembly (5), guide ball (14), guide plate (15), and dowel pins (56) as a unit.
7. Place the barrel (3) on a clean cloth or plastic film. Hold the side of the guide plate (15) and gently remove the piston assembly.
8. Remove the guide ball (14) and dowel pins (56).
9. Place the pump body (1), shaft down, on a fixture designed to keep it from toppling. Protect with a dust­proof plastic film.
10. Place the cover (2) with the assembled guide sleeve (64), plunger (21) and needle bearing (65) on a work bench. The guide sleeve must face up. Protect the parts with a dust-proof plastic film.
NOTE: Following completion of disassembly procedure steps 1 through 10, necessary pump inspection can be performed. Further disassembly may be required if the following inspection steps reveal specific problems.
11-1. When the barrel (3) is laid flat, the dowel pins (56) must protrude slightly. If otherwise, or if the dowel pins are easily pushed in, replace the barrel.
Case Drain
Ports
Figure 4
11-2. If the hanger (9) has little or no inclination against the shaft (8), or if it can easily be moved by hand, go to steps 12 through 15.
11-3. If shaft seal leakage or excessive ball-bearing play is apparent, go to steps 16 through 21.
11-4. If compensator function is erratic, go to steps 23 through 33, as required.
Hanger Removal
12. Place the pump body in a large vise, or on a working surface adapted to hold the pump body firmly.
13. Remove the trunnions (10) using the blind threaded holes, and the appropriate trunnion removal tool. See Figure 9 on page 13 for trunnion removal
tool specifications.
CAUTION: The hanger may be under tension, and should be secured to prevent injury.
14. Remove the hanger (9), spring seat (20), and spring (19) in this order.
15. Proceed to HANGER INSPECTION and TRUNNION INSPECTION, page 9.
Shaft Removal and Disassembly
16. As required, remove the key (70). Tap gently at the end of the key with a hammer or chisel if it is difficult to remove.
17. Remove the retaining ring (41) with a snap ring pliers.
18. Remove the shaft (8). Pull the shaft toward the cover. Tap lightly with a fiber hammer on the end of the shaft if it is difficult to remove.
19. Replace the ball-bearing if it shows excessive wear, or if noise is heard when rotating the outer race by hand.
20. To replace the ball bearing, remove retaining rings (68), and remove the ball bearing (69) with a hand press or by light hammering.
21. If oil leaks are observed, the shaft seal must be replaced. Remove the shaft seal (38) from the pump body (1). Use a push rod of smaller diameter than the outside diameter of the shaft seal.
NOTE: Do not reuse seals. See Parts List, page 17, Item 38 for replacement part numbers.
22. Proceed to SHAFT INSPECTION, page 9, and BALL BEARING INSPECTION, page 11.
Compensator Disassembly
23. Loosen the hex nut (28-12) and remove the adjusting screw (28-11) from the end cap (28-3).
24. Remove the end cap (28-3).
25. Remove the spring (28-6) and spring seat (28-5).
26. Remove the spool (28-2). Continue for Codes 7, 19, and 26 compensators.
Item numbers refer to figures 16 and 17, page 20.
27. Loosen the hex nut (12) and remove the adjusting screw (18) from the body (1).
28. Remove the spring (7) and cone (16).
29. Proceed to PRESSURE COMPENSATOR INSPECTION, page 11.
6
Form No. R92.00 Rev. 10/03
HPV REPAIR PROCEDURES (continued)
NOTE: If the cone is badly worn or damaged, perform the following steps.
30. For Code 7 or 19 compensators, remove the plug (20). Using a rod, tap the seat (15) out from the opposite end.
31. For Code 26 compensators, remove the fitting (27) and adjusting screw (18) as an assembly.
32. Remove the dowel pin (24) and ball (17).
33. Remove the fitting (29). Using a rod, tap the seat (15) out from the opposite end.
Rework Limits for Wear Parts
Barrel Bores Measure each bore in four places, including one place deep within the bore, where the piston doesn’t run. Replace the barrel if the difference in measurements exceeds .0004 in. or .010 mm.
Barrel Face May be lapped no more than .0002 in. or .005 mm measured by before and after depths of oil grooves on barrel face.
Pistons (5) Measure each piston in four places, including one at the shoe end, where the piston doesn’t enter the barrel. Replace Piston if the difference in measurements exceeds .0006 in. or .015 mm.
Shoe, Piston Assembly Replace assemblies if end play exceeds .003 in. or .076 mm.
Shoe, Face May be lapped up to .004 in. or .102 mm. The difference in shoe flange thickness between the thinnest and thickest of nine shoes should not exceed .0012 in. or. 03 mm.
Port Plate (4) May be lapped .006 in. or .152 mm. Maintain flatness of .0002 in. or .005 mm.
Wear Plate (16) Do not lap. Replace if there are any indications of wear or bending.
Guide Plate (15) Do not lap. Measure thickness at several places. Replace if thickness varies more than .004 in. or .102 mm.
INSPECTION PROCEDURES
Part (Item No.) Inspection Procedure Corrective Action
Check for cracks around tapped holes.
Pump Body Check for cracks around retainer ring groove. Replace if cracked.
(1) Perform dye penetrant or magnetic particle inspection over
entire housing when oil leakage is observed.
Visually inspect for obvious defects Check for excessive wear in guide sleeve (64). Axial scratches
should not be detectable with a fingernail. Diameter difference
Cover must not exceed .001 in. or .025 mm when measured at several Replace if defective
(2) random points.
Check for excessive play between drive shaft (8) and needle
bearing (65). (Maximum radial play is .003 in. or .076 mm.)
Repair by lapping until
Visually inspect the barrel face for uniform minute concentric nicks. scratches are removed.
Do not exceed rework
limits listed above.
Visually inspect for deep, localized nicks. Replace barrel. Flush
Barrel reservoir and circuit.
(3) Replace barrel.
Check for
Visually inspect for signs of seizure, scoring or discoloration. correct hydraulic fluid
type, temperature rise,
excessive pressure.
Correct as needed.
Form No. R92.00 Rev. 10/03
Continued on Page 8
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