Choosing a replacement or upgrade pump is an arithmetic problem before it is a catalogue problem. Displacement, speed, pressure and duty cycle define what the machine needs; the series and frame size that satisfy those numbers are then a short list rather than a catalogue sweep.
This article works through the calculation in the order a buyer should actually use it, then maps the result onto the pump families commonly fitted to excavators and industrial equipment.
Every pump decision reduces to the same four quantities. Confusing them is the most common cause of buying a pump that is either oversized, overheated or permanently at its pressure ceiling.
| Quantity | Symbol | Meaning | Where you find it |
|---|---|---|---|
| Displacement | Vg | Oil volume per shaft revolution | Nameplate, in cm³/rev or ml/r |
| Shaft speed | n | Revolutions per minute at working load | Engine speed through the drive ratio |
| Working pressure | p | Continuous operating pressure, not peak | System specification |
| Flow | Q | Volume delivered per minute | Calculated, then measured |
The relationship is direct: flow in litres per minute equals displacement in cm³/rev multiplied by speed in rpm, divided by 1000. A 71 cm³ pump turning at 2,000 rpm delivers about 142 L/min at 100 percent volumetric efficiency, and in practice perhaps 130–135 L/min once leakage and temperature are accounted for.
Buyers frequently compare pumps using a single "max pressure" figure and are then surprised when a pump rated at 350 bar fails in service. Manufacturers publish at least three ratings, and only the first matters for continuous duty.
| Rating | What it means | How it is used |
|---|---|---|
| Nominal / continuous | Sustainable for the full service life at rated speed | The design point for the application |
| Peak / intermittent | Allowed briefly, typically seconds, and limited in total hours | Relief settings, stall events |
| Proof / static | One-off test pressure without damage | Component testing, not operation |
A pump with a 400 bar peak rating and a 315 bar continuous rating should be specified at 315 bar or below unless the duty cycle genuinely spends most of its life at low pressure. Relief valves set at the peak figure are a common and expensive mistake — they convert every overload into a full-pressure event on the rotating group.
Hydraulic power in kilowatts equals pressure in bar multiplied by flow in litres per minute, divided by 600. Shaft torque in newton-metres equals displacement in cm³/rev multiplied by pressure in bar, divided by 63.6.
Both figures matter commercially. If a proposed pump needs more torque than the engine can deliver at the operating point, the machine will bog rather than dig, and the pump will spend its life at the torque limiter. If the pump is too small, the machine is slow and the operator compensates by raising relief pressure, which shortens pump life. The correct specification satisfies flow demand at an engine speed where torque is available, with a margin for the implements.
Tonnage is not a specification, but it is a useful first filter because machine classes cluster around similar hydraulic demands. The table below is an orientation guide, not a substitute for the nameplate.
| Machine class | Typical main pump displacement | System pressure band | Typical series |
|---|---|---|---|
| Mini excavator, 1–4 t | 10–30 cm³/rev per pump | 200–250 bar | Small variable axial pumps |
| Compact, 5–8 t | 40–63 cm³/rev | 250–300 bar | K3V63, A10VO45–63 |
| Mid size, 13–22 t | 112–140 cm³/rev | 300–350 bar | K3V112, K5V140, A10VSO71–125 |
| Large, 25–40 t | 160–210 cm³/rev | 320–350 bar | K5V160–200, HPV165–210 |
| Mining class, 45 t and above | 250–280 cm³/rev | 350 bar and above | K5V200+, HPV280, A4VSO250+ |
Use the table to narrow the search, then confirm against the actual machine: number of pumps, whether the circuit is open or closed, whether the swing and travel functions share the main pump, and the relief settings recorded on the valve block.
Two machines of identical tonnage can require different pumps because the work differs. A breaker-equipped excavator spends much of its life at high pressure with low flow demand; a trenching machine runs high flow at moderate pressure for hours. The first needs pressure capability and good low-flow efficiency; the second needs flow at sustained speed and attention to heat rejection.
Three practical rules follow from this. Size for the duty cycle rather than the peak, keep continuous pressure at least 10 percent below the rating, and check that reservoir and cooler capacity can absorb the actual heat load — roughly the input power minus useful work, which at typical efficiencies is a fifth to a quarter of installed power.
A pump that is correctly specified on paper can still be wrong on the machine, so verify three readings in the first week of service.
| Reading | How to take it | Expected result |
|---|---|---|
| Flow at working pressure | Inline meter, oil at 50–60 °C | Within about 10 percent of calculated output |
| Case drain flow | Drain return, warm oil, rated pressure | Within the manufacturer limit for the frame size |
| Stabilised oil temperature | Reservoir, after one hour of work | Within the system design band, not climbing |
If flow is low, check speed first and leakage second. If temperature climbs steadily, the pump is generating more heat than the cooler can reject — usually because continuous pressure is closer to the peak rating than intended. Catching either within the first week prevents the failure that would otherwise appear at the end of the season.
Once the numbers are fixed, the shortlist is usually obvious. For open-circuit excavator main pumps, the Kawasaki K5V family is the reference point and parts for K5V80, K5V140, K5V160 and K5V200 units cover the mid to large classes. Where the machine uses a Linde HPV installation, HPV55 through HPV280 pumps span compact to mining sizes with a consistent control architecture. For closed-circuit drives and industrial applications, the Rexroth A4VG range is served by parts for A4VG28 to A4VG250 frame sizes across both open and closed circuit variants.
To confirm a selection, send the pump model and nameplate data from the machine, the part numbers of any existing components, the machine model and serial number, and the quantity required. With those we verify displacement, control type and mounting pattern against the drawings — the three details that most often turn a "same size" pump into a pump that does not fit.
Only if the engine torque, relief settings, cooler capacity and line sizes support the extra flow. Increasing displacement without those changes usually produces heat and stall rather than productivity.
Open circuit pumps draw from the reservoir and return oil there. Closed circuit pumps work in a loop with a charge pump and are used for hydrostatic drives, typically travel and winch functions.
Because control type, maximum displacement setting and speed limit differ between variants. The suffix after the frame size is part of the specification, not decoration.
Size flow for the implement demand at working engine speed, keep continuous pressure at least 10 percent below the rating, and confirm the cooler can reject the resulting heat at the highest ambient temperature expected.
Choosing a replacement or upgrade pump is an arithmetic problem before it is a catalogue problem. Displacement, speed, pressure and duty cycle define what the machine needs; the series and frame size that satisfy those numbers are then a short list rather than a catalogue sweep.
This article works through the calculation in the order a buyer should actually use it, then maps the result onto the pump families commonly fitted to excavators and industrial equipment.
Every pump decision reduces to the same four quantities. Confusing them is the most common cause of buying a pump that is either oversized, overheated or permanently at its pressure ceiling.
| Quantity | Symbol | Meaning | Where you find it |
|---|---|---|---|
| Displacement | Vg | Oil volume per shaft revolution | Nameplate, in cm³/rev or ml/r |
| Shaft speed | n | Revolutions per minute at working load | Engine speed through the drive ratio |
| Working pressure | p | Continuous operating pressure, not peak | System specification |
| Flow | Q | Volume delivered per minute | Calculated, then measured |
The relationship is direct: flow in litres per minute equals displacement in cm³/rev multiplied by speed in rpm, divided by 1000. A 71 cm³ pump turning at 2,000 rpm delivers about 142 L/min at 100 percent volumetric efficiency, and in practice perhaps 130–135 L/min once leakage and temperature are accounted for.
Buyers frequently compare pumps using a single "max pressure" figure and are then surprised when a pump rated at 350 bar fails in service. Manufacturers publish at least three ratings, and only the first matters for continuous duty.
| Rating | What it means | How it is used |
|---|---|---|
| Nominal / continuous | Sustainable for the full service life at rated speed | The design point for the application |
| Peak / intermittent | Allowed briefly, typically seconds, and limited in total hours | Relief settings, stall events |
| Proof / static | One-off test pressure without damage | Component testing, not operation |
A pump with a 400 bar peak rating and a 315 bar continuous rating should be specified at 315 bar or below unless the duty cycle genuinely spends most of its life at low pressure. Relief valves set at the peak figure are a common and expensive mistake — they convert every overload into a full-pressure event on the rotating group.
Hydraulic power in kilowatts equals pressure in bar multiplied by flow in litres per minute, divided by 600. Shaft torque in newton-metres equals displacement in cm³/rev multiplied by pressure in bar, divided by 63.6.
Both figures matter commercially. If a proposed pump needs more torque than the engine can deliver at the operating point, the machine will bog rather than dig, and the pump will spend its life at the torque limiter. If the pump is too small, the machine is slow and the operator compensates by raising relief pressure, which shortens pump life. The correct specification satisfies flow demand at an engine speed where torque is available, with a margin for the implements.
Tonnage is not a specification, but it is a useful first filter because machine classes cluster around similar hydraulic demands. The table below is an orientation guide, not a substitute for the nameplate.
| Machine class | Typical main pump displacement | System pressure band | Typical series |
|---|---|---|---|
| Mini excavator, 1–4 t | 10–30 cm³/rev per pump | 200–250 bar | Small variable axial pumps |
| Compact, 5–8 t | 40–63 cm³/rev | 250–300 bar | K3V63, A10VO45–63 |
| Mid size, 13–22 t | 112–140 cm³/rev | 300–350 bar | K3V112, K5V140, A10VSO71–125 |
| Large, 25–40 t | 160–210 cm³/rev | 320–350 bar | K5V160–200, HPV165–210 |
| Mining class, 45 t and above | 250–280 cm³/rev | 350 bar and above | K5V200+, HPV280, A4VSO250+ |
Use the table to narrow the search, then confirm against the actual machine: number of pumps, whether the circuit is open or closed, whether the swing and travel functions share the main pump, and the relief settings recorded on the valve block.
Two machines of identical tonnage can require different pumps because the work differs. A breaker-equipped excavator spends much of its life at high pressure with low flow demand; a trenching machine runs high flow at moderate pressure for hours. The first needs pressure capability and good low-flow efficiency; the second needs flow at sustained speed and attention to heat rejection.
Three practical rules follow from this. Size for the duty cycle rather than the peak, keep continuous pressure at least 10 percent below the rating, and check that reservoir and cooler capacity can absorb the actual heat load — roughly the input power minus useful work, which at typical efficiencies is a fifth to a quarter of installed power.
A pump that is correctly specified on paper can still be wrong on the machine, so verify three readings in the first week of service.
| Reading | How to take it | Expected result |
|---|---|---|
| Flow at working pressure | Inline meter, oil at 50–60 °C | Within about 10 percent of calculated output |
| Case drain flow | Drain return, warm oil, rated pressure | Within the manufacturer limit for the frame size |
| Stabilised oil temperature | Reservoir, after one hour of work | Within the system design band, not climbing |
If flow is low, check speed first and leakage second. If temperature climbs steadily, the pump is generating more heat than the cooler can reject — usually because continuous pressure is closer to the peak rating than intended. Catching either within the first week prevents the failure that would otherwise appear at the end of the season.
Once the numbers are fixed, the shortlist is usually obvious. For open-circuit excavator main pumps, the Kawasaki K5V family is the reference point and parts for K5V80, K5V140, K5V160 and K5V200 units cover the mid to large classes. Where the machine uses a Linde HPV installation, HPV55 through HPV280 pumps span compact to mining sizes with a consistent control architecture. For closed-circuit drives and industrial applications, the Rexroth A4VG range is served by parts for A4VG28 to A4VG250 frame sizes across both open and closed circuit variants.
To confirm a selection, send the pump model and nameplate data from the machine, the part numbers of any existing components, the machine model and serial number, and the quantity required. With those we verify displacement, control type and mounting pattern against the drawings — the three details that most often turn a "same size" pump into a pump that does not fit.
Only if the engine torque, relief settings, cooler capacity and line sizes support the extra flow. Increasing displacement without those changes usually produces heat and stall rather than productivity.
Open circuit pumps draw from the reservoir and return oil there. Closed circuit pumps work in a loop with a charge pump and are used for hydrostatic drives, typically travel and winch functions.
Because control type, maximum displacement setting and speed limit differ between variants. The suffix after the frame size is part of the specification, not decoration.
Size flow for the implement demand at working engine speed, keep continuous pressure at least 10 percent below the rating, and confirm the cooler can reject the resulting heat at the highest ambient temperature expected.
