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relief valve must be set to relieve at a pressure 
equal to or below the rated capability of the lowest 
rated component. 

 

Before starting the pump every time, check to 
insure: 

•  The pressure relief valve is in good 

operating condition and has been set to the 
proper relief pressure. 

• 

Any pipe line used to direct pressurized relief 
flow to another location, such as a collecting 
tank, is not blocked. 

• 

The discharge system is not blocked and all 
the discharge line valves are open. 

 

Check all fluid end discharge system 
components including pipe, connections, 
elbows, threads, fasteners, hoses, etc., at least 
once every six months to confirm their 
structural adequacy.

  With time, wear, corrosion 

and fatigue can reduce the strength of all 
components.  Magnetic iron and steel components 
should be checked with magnetic particle or dye 
penetrate crack detection equipment.  Nonmagnetic 
materials should be checked for cracks with dye 
penetrants.  All metallic components should also be 
visually checked during these inspections for signs 
of corrosion.  If a component shows evidence of 
cracking or loss of material due to corrosion it must 
be replaced with a new part. 

 
Continually monitor suction and discharge hose 
assemblies when the pump is operating for leakage, 
kinking, abrasion, corrosion or any other signs of 
wear or damage. 

 

Worn or damaged hose assemblies should be 
replaced immediately.

  At least every six months 

examine hose assemblies internally for cut or 
bulged tube, obstructions and cleanliness.  For 
segment style fittings, be sure that the hose butts up 
against the nipple shoulder, the band and retaining 
ring are properly set and tight and the segments are 
properly spaced.  Check for proper gap between nut 
and socket or hex and socket.  Nuts should swivel 
freely.  Check the layline of the hose to be sure that 
the assembly is not twisted.  Cap the ends of the 
hose with plastic covers to keep them clean until 
they are tested or reinstalled on the pump unit.  
Following this visual examination, the hose 
assembly should be hydrostatically tested, on test 
stands having adequate guards to protect the 
operator, per the hose manufacturer’s proof test 
procedure. 

 

Fluid end component inspections should be 
performed more frequently than every six 
months if pressures above 2,500 PSI are used in 
the discharge system or if corrosive, flammable 
or hot  (over 110º F) fluids are being pumped.  

 

Before starting the pump the first time and 
periodically thereafter check the pump, suction and 
discharge system fastener torques versus the 
values listed on page 26 to insure proper tightness. 

   
Over and under torquing can damage threaded 
pipes, connections and fasteners, which may lead 
to component damage and/or failure.  Replace all 
components found to be damaged or defective.   

 
Block the crankshaft from turning and make certain 
that all pump drive motor or engine start switches or 
starter controls are clearly tagged with warnings not 
to start the pump while repair work is in process. 

 
Whenever the pump is operating, continually 
monitor the entire suction, discharge and pump 
lubricating systems for leaks.  Thoroughly 
investigate the cause for leakage and do not 
operate the pump until the cause of the leak has 
been corrected.  Replace any parts which are found 
to be damaged or defective.  When a gasketed joint 
is disassembled for any reason, discard the used 
gasket and replace it with a new, genuine Gardner 
Denver gasket before reassembling the joint. 

 
Due to the high working pressures contained by the 
fluid cylinder, discharge manifold and discharge 
piping, welding on these components is not 
recommended.  If welding on the discharge system 
cannot be avoided, only experienced, qualified 
welders should be used.  In addition, the welded 
part should be hydrostatically proof tested in the 
shop with water or hydraulic fluid to one and one 
half times maximum discharge system working 
pressure, with no observable fluid leakage, before 
the part is reinstalled in the pump system. 

 
In summary, high pressure fluid streams can 
possess sufficient energy to cause personal injury, 
death and/or equipment damage.  These results 
can occur either through direct contact with the fluid 
stream or by contact with loose objects the fluid 
stream has propelled, if the pump system is 
improperly used, or if the fluid is misdirected, or 
allowed to escape from defective or improperly 
maintained equipment. 

  

 DANGER 

 

Do not attempt to service, repair, adjust or 
otherwise work on the pump while the 
unit is operating.  Shut off the pump drive 
motor or engine and relieve the fluid 
pressure in the pump suction and 
discharge systems before any work or 
investigation is performed on the pump or 
pump systems. 

Содержание GD-250

Страница 1: ...GARDNER DENVER 3 1 618 Version 1 January 2011 TRIPLEX PISTON PUMP 5 STROKE MODEL GD 250 WELL SERVICE OPERATING AND SERVICE MANUAL Rental Pump Supplied By...

Страница 2: ...ed distributor service technicians are factory trained and skilled in pump maintenance and repair They are ready to respond and assist you by providing fast expert maintenance and repair services For...

Страница 3: ...operation and minimum downtime DANGER Danger is used to indicate the presence of a hazard which will cause severe personal injury death or substantial property damage if the warning is ignored WARNIN...

Страница 4: ...tions 7 Crankcase Oil Requirements 16 Gardner Denver Horizontal Pump Recommended System Layout for Proper Performance 16 Net Positive Suction Head Required NPSHR at Fluid Cylinder Suction Connection w...

Страница 5: ...ting and Cleaning Danger Notice 5 6 Hydraulic Puller Danger Notice 2 INSTALLATION AND OPERATING INSTRUCTIONS SECTION 2 7 Lifting and Moving Equipment Danger Notice 2 Location 7 Lubrication Packing 12...

Страница 6: ...or Temperature Correction Char 21 Wedge Puller Danger Notice 2 LIST OF ILLUSTRATIONS Figure Description Page Figure 1 View of the Eccentric thru the Hood Opening Step 1 18 Figure 2 View of the Eccent...

Страница 7: ...g and service manuals should be readily available for operator and maintenance personnel use Read and follow all the precautions and instructions contained in these manuals If any of these documents a...

Страница 8: ...e handle to avoid losing control of the hammer while swinging and striking Carefully swing the hammer to avoid striking themselves another person and objects other than the targeted wedge Avoid swingi...

Страница 9: ...o lift a pump package unit subassemblies or individual components and you observe the equipment is tilting or appears unbalanced lower the equipment and adjust the lifting device to eliminate these im...

Страница 10: ...han every six months if pressures above 2 500 PSI are used in the discharge system or if corrosive flammable or hot over 110 F fluids are being pumped Before starting the pump the first time and perio...

Страница 11: ...s must be taken to avoid possible personal injury death and or equipment damage from explosion fire or burns HIGH PRESSURE LIQUID JETTING BLASTING AND CLEANING Pressure or flow directing devices often...

Страница 12: ...tion These components should all be tagged with their tested pressure capabilities together with the date testing was performed Always be aware of the pressure level in the system and never connect an...

Страница 13: ...supported independently of the pump to insure that no strain is imposed in the pump by misalignment or improperly fitted pipe PRESSURE RELIEF VALVE The pump must be protected from excessive discharge...

Страница 14: ...f care is taken to stay within the listed temperature ranges Straight weight oils are also ideal in pumps used indoors when ambient temperatures are controlled The oil level in the pump should be chec...

Страница 15: ...the crankcase Drain all water accumulation from the bottom of crankcase Check all nuts and screws and tighten if necessary Fill crankcase with oil of proper grade to proper level Quantity on the data...

Страница 16: ...th a valve seat puller Wipe the tapered surface of the valve seat and pump valve deck in the fluid cylinder with a clean cloth Lower the seat into the port taper and then lift slightly and drop If the...

Страница 17: ...nd rust in the stuffing box pilot bores in the frame Install the packing in the box Place a new gasket in the stuffing box groove The gasket chamfered edge must face out to prevent gasket pinching whe...

Страница 18: ...e placed over a lock pin which has been inserted in a lock pin hole in the gland When using self adjusting packing tighten the gland nut firmly after assembling it metal to metal with the stuffing box...

Страница 19: ...ot contaminate the crankcase oil CROSSHEAD AND PINS Crossheads can be removed through the oil stop head openings Crossheads are equipped with straight pins secured on each end by setscrews and locknut...

Страница 20: ...re Tighten oil stop head gland to prevent seal movement while pump is in operation These oil stop head seals are nonadjustable When crankcase oil leakage occurs past seals the seals should be replaced...

Страница 21: ...the crankcase the oil and filter should be changed Drain and clean out the crankcase before putting in new oil Replace the oil stop head seals before running the pump We recommend oil stop head seals...

Страница 22: ...e or grade used A crankcase heater and or an oil heat exchanger may be needed to meet these requirements Crankcase capacity is 12 gallons 45 4 liters WARNING Failure to follow these lubrication requir...

Страница 23: ...y into tank outlet 4 A short straight suction line is preferred from the tank to the pump If this is not possible use as few bends as possible and use long radius elbows The smallest portion of the li...

Страница 24: ...3 1 618 Page 18 FIGURE 1 STEP 1 FIGURE 2 STEP 2...

Страница 25: ...3 1 618 Page 19 FIGURE 3 STEP 3 FIGURE 4 STEP 4...

Страница 26: ...d minimum plunger sizes Interpolate between NPSH curves for each plunger size NPSHR is defined at a 3 flow drop below maximum capacity Added suction head above that shown by the curves must be provide...

Страница 27: ...3 1 618 Page 21 CORRECTION CHART FOR TEMPERATURE OR VISCOSITY...

Страница 28: ...0 592 64 60 20 45 40 3 106 0 35 9 0 3 9 67 45 800 176 81 00 677 73 80 23 35 35 2 120 0 39 9 8 4 1 74 50 900 198 91 00 762 83 00 26 30 31 3 135 0 41 10 7 4 3 82 58 1000 220 100 7 896 92 10 29 20 28 2 1...

Страница 29: ...mbly 2 Valve propped open 2 Remove prop 3 Pump cavitating 3 See Cavitation Fluid Knock or Hammer problem 4 Fluid leakage 4 Replace fluid end seals 5 Erroneous gauge reading 5 Recalibrate or replace ga...

Страница 30: ...13 Multiple pumps operating in 13 Use a suction stabilizer phase on each pump Separate lines may also be needed Suction or Discharge Line Vibration 1 Line s not supported 1 Install supports or hangers...

Страница 31: ...il stop head packing 2 Replace packing 3 Oil level too high in 3 Reduce oil level crankcase 4 Excessive crosshead wear 4 Replace crosshead 5 Pressure in crankcase 5 Clean or replace air breather Oil S...

Страница 32: ...temperature 5 Lube oil pump failure 5 Replace oil pump 6 Low oil level in sump 6 Check oil level frequently and add oil as required 7 Contaminated oil in sump 7 Check oil condition frequently 8 Cavita...

Страница 33: ...ad Pin 2 0015 2 0020 50 838 50 851 Bore in Connecting Rod Bushing for Eccentric 10 499 10 505 266 675 266 827 Crosshead Pin Diameter 2 0005 2 0000 50 8127 50 8000 Bore in Crosshead for Pin 2 0010 2 00...

Страница 34: ...Service Department Telephone 800 682 9868 FAX 217 223 1581 For Domestic parts information Contact Gardner Denver Fluid Transfer Division 2200 South Prospect Oklahoma City OK 73129 Telephone 405 677 57...

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