• No results found

Axial Piston Variable Pump KVA

N/A
N/A
Protected

Academic year: 2021

Share "Axial Piston Variable Pump KVA"

Copied!
16
0
0

Loading.... (view fulltext now)

Full text

(1)

Axial Piston Variable Pump

KVA

Technical data sheet

Series 6

Sizes 55 ... 107

Nominal pressure 300 bar

Peak pressure 350 bar

for commercial vehicles, open circuit

Features

– Variable pump with axial tapered piston rotary group of bent axis design. Designed especially to meet the requirements of commercial vehicles.

– The output flow is proportional to the drive speed and pump displacement and is steplessly variable between maximum and zero (qv max to qv min = 0).

– Favourable power/weight ratio, small overall dimensions, optimum efficiency and economic design

– Self aspirating, for open circuit operation

– Flange and shaft designed for direct mounting on truck gear-box PTO‘s

– Further Informations:

Fixed pump KFA _________________________ RE 91501 designed especially to meet the requirements of commercial vehicles.

RE 92250/02.07 /16

Replaces: 04.06

Contents

Ordering Code / Standard Program 2

Technical Data 3

DRS - Pressure Control with Load Sensing 6 EP - Electric Control with Proportional Solenoid 7

Unit Dimensions, Size 55 8

Unit Dimensions, Size 80 10

Unit Dimensions, Size 107 12

Installation Notes 14

(2)

Ordering Code / Standard Program

Axial piston unit

01 Bent axis design, variable, nominal pressure 300 bar, peak pressure 350 bar,

for commercial vehicles (truck) KVA7V

Operation mode

02 Pump in open circuits O

Size

03 ≈ Displacement Vg max in cm3 55 80 07

Control devices 55 80 07

04

Pressure control with load sensing    DRS

Electric control with proportional solenoid U = 24 V positive characteristics  – – EP2

negative characteristics – –  EP4

Series

05 6

Index

06 3

Direction of rotation

07 Viewed on shaft end clockwise R

counter-clockwise L

Seals

08 FKM (2 back to back shaft seals) M

Shaft end

09 Splined shaft similar DIN ISO 14 (for truck use) E

Mounting flange

10 Special flange ISO 7653-1985 (for truck use) K

Service line ports

11 Threaded port A(B), rear 64

 = available – = not available

KVA7V

O

/

6

3

M

E

K

64

(3)

Technical Data

Hydraulic fluid

Before starting project planning, please refer to our data sheets RE 90220 (mineral oil) and RE 90221 (environmentally acceptable hydraulic fluids) for detailed information regarding the choice of hydraulic fluids and conditions of use.

If environmentally acceptable hydraulic fluids are being used, the limitations regarding technical data and seals mentioned in RE 90221 must be observed.

When ordering please indicate the used hydraulic fluid.

Attention:

For the operation with water-containing HF-fluids the variable pump KVA is not suitable.

Viscosity range

We recommend that a viscosity (at operating temperature) for optimum efficiency and service life purposes of

νopt = opt. operating viscosity 16...36 mm2/s

be chosen, taken the tank temperature (open circuits) into account.

Limits of viscosity range

The following values apply in extreme cases: νmin = 5 mm2/s

short term (t < 3 min.) at max. permitted temperature tmax = 115°C.

νmax = 1600 mm2/s

short term (t < 3 min.) with cold start (p < 30 bar, n ≤ 1000 rpm,tmin = -25°C).

Note that the maximum hydraulic fluid temperature of 115°C must not be exceeded locally either (e.g. bearing area). The temperature in the bearing area is - depending on pressure and speed - up to 12 K higher than the average case drain tempe-rature.

This axial piston unit can not be operated in a temperature range of less than -25°C.

Selection diagram tmin = -25°C tmax = +115°C -40° -25° -10° 0° 10° 30° 50° 70° 90° 115° 5 10 40 60 20 100 200 400 600 1000 1600 -40° -20° 0° 20° 40° 60° 80° 100° 1600 nopt. 16 36 VG 22 VG 32 VG 46 VG 6 8 VG 1 00 5

hydraulic fluid temperature range

temperature t in °C

viscosity

ν in mm

2/s

Details regarding the choice of hydraulic fluid

The correct selection of hydraulic fluid requires knowledge of the operating temperature in relation to the ambient tempera-ture, in an open circuit the tank temperature.

The hydraulic fluid should be selected so that within the operating temperature range, the operating viscosity lies within the optimum range (νopt) (see shaded section of the selection

diagram). We recommend that the highest possible viscosity range should be chosen in each case.

Example: At an ambient temperature of X° C an operating tem-perature of 60° C is set in the circuit. In the optimum viscosity range (νopt; shaded area) this corresponds to the viscosity

classes VG 46 or VG 68; to be selected: VG 68.

Please note: The case drain temperature, which is affected by

pressure and rotational speed, is always higher than the tank temperature. At no point in the system may the temperature be higher than 115°C.

If this cannot be achieved due to unusual operating parameters or high ambient temperatures, please contact us.

Filtration

The finer the filtration, the cleaner the fluid and the longer the service life of the axial piston unit.

To ensure proper function of the axial piston unit, the hydraulic fluid must have a cleanliness level of at least

20/18/15 according to ISO 4406.

At very high hydraulic fluid temperatures (90°C to max. 115°C), a cleanliness level of at least

19/17/14 according to ISO 4406 is required. Please contact us, if these cleanliness levels cannot be achie-ved.

(4)

Technical Data

Operating pressure range

Inlet

Pressure at port S

The minimum inlet pressure depends on the speed. The following limits may not be exceeded.

pabs min ______________________________________ 0,8 bar

The maximum pressure pabs max also depends on speed (see

succeeding diagram).

Minimum inlet pressure at

suction port S with increased speed

In order to avoid damage of the pump a minimum inlet pressure at the suction port must be assured. The minimum inlet pres-sure is related to the rotational speed and the displacement of the variable pump.

0,6 0,7 0,8 0,9 1,0 2,0 1,8 1,6 1,4 1,2 1,1 1,0 0,9 0,8 1,9 1,7 1,5 1,3 1,5 1,4 1,3 1,2 1,1 1,0 0,9 0,8 n nmax 1 Vg Vg max Displacement Inlet pressure p abs in bar Speed Note:

– max. permissible speed nmax perm. (speed limit, see page 5)

– min. and max. permissible inlet pressure at port S

Outlet

Maximum pressure at port A or B

(pressure specifications in according to DIN 24312) Nominal pressure pN _________________________ 300 bar

Peak pressure pmax __________________________ 350 bar

Case drain

The case of the pump is connected to the inlet port. A separate case drain is therefore not required (purge port R is plugged)

Exception:

When using the DRS control a separate drain line from port T to the tank is mandatory (not required for EP control).

Temperature range

The FKM shaft seal ring is admissible for a case temperature range from -25°C bis +115°C.

Note:

This axial piston unit can not be operated in a temperature range of less than -25°C.

Direction of flow

Direction of rotation, viewed on shaft end

clockwise counter-clockwise

(5)

Table of values

(theoretical values, without efficiencies and tolerances; values rounded)

Size 55 80 07

Displacement Vg max cm3 54,8 80 107

Speed max. 1)

at Vg max nmax1 rpm 2500 2240 2150

at Vg < 0,74 • Vg max (see diagram, page 4) nmax2 rpm 3400 3000 2900

Speed max. 2) nmax perm. rpm 3750 3350 3200

Flow at nmax 1 and Vg max qv max 1 L/min 137 179 230

Power at qv max 1 and Δp = 300 bar Pmax 1 kW 68 90 115

Torque at Vg max and Δp = 300 bar T Nm 261 382 510

Mass moment TG Nm 21 28,5 41

Moment of inertia (of the rotating parts) J kgm2 0,0034 0,0064 0,0102

Filling capacity V L 0,6 0,8 1,2

Mass (approx.) m kg 16 20 24

1) The values shown are valid for an absolute pressure pabs = 1 bar at the suction port »S« and when operated on mineral fluid

with a specific mass of 0,88 kg/L.

2) Maximum speed (speed limit) for an increase in the inlet pressure pabs at the suction port S and Vg < Vg max

Determining the size

Flow qv= Vg • n • ηv L/min 1000 Torque T = Vg • Δp Nm 20 • π • ηmh Power P = 2 π • T • n = qv • Δp kW 60000 600 • ηt

Permissible axial loading on the drive shaft

The values given are maximum values and do not apply to continous operation. For drives with radial loading (pinion, V-belt drives), please contact us!

Size 55 80 07

when stopped or when axial piston unit

working in pressureless conditions ± Fax max N 0 0 0

Axial force / operating pressure Fax – + + Fax zul. − Fax zul. N/bar 8,7 10,6 12,9 N/bar -66 -86 -103

When considering the permissible axial force, the force-transfer direction must be taken into account: − Fax max = increase in service life of bearings

+ Fax max = reduction in service life of bearings (avoid if at all possible)

Accessories for KVA

For the KVA-pump the following accessories are available from Rexroth: – Coupling flange, used in pump operation via a joint shaft (see RE 95001) – Suction pipe, in all variations (see RE 95004)

– Adaption flange, for KVA-mounting in unfavourable mounting conditions (on enquiry)

Technical Data

Vg = Displacement per revolution in cm3

Δp = Differential pressure in bar n = speed in rpm

ηv = Volumetric efficiency

ηmh = Mechanical-hydraulic efficiency

(6)

DRS - Pressure Control with Load Sensing

Function of the pressure control

The pressure control keeps the pressure in a hydraulic system constant within its control range even under varying flow condi-tions. The variable pump only moves as much hydraulic fluid as is required by the actuators. If the operating pressure exceeds the setpoint set at the integral pressure control valve, the pump displacement is automatically swivelled back until the pressure deviation is corrected.

In zero pressure non-running condition, the pump is swivelled to its starting position Vg max by means of the control spring.

Setting range for pressure control _________ 80 to 320 bar Standard setting: ____________________________ 300 bar

Note:

Any pressure relief vlave included in the circuit to limit the max. pressure must be set to a cracking pressure at least 20 bar above the pressure control setting.

The pressure control is superimposed on the load sensing valve, i.e. the load sensing function operates below the set pressure.

Load sense function

The load sensing control is a flow control option that operates as a function of the load pressure to regulate the pump dis-placement to match the actuator flow requirement.

The flow depends here on the cross section of the external sensing orifice (1) fitted between the pump outlet and the actuator. The flow is independent of the load pressure below the pressure cut-off setting and within the control range of the pump.

The sensing orifice is usually a separately arranged load sensing directional valve (control block). The position of the directional valve piston determines the opening cross section of the sensing orifice and thus the flow of the pump.

The load sensing control compares pressure before and after the sensing orifice and maintains the pressure drop across the orifice - and therefore the pump flow - constant as a function of the orifice size.

If the differential pressure Δp increases, the pump is swivel-led back towards Vg min and, if the Δp decreases the pump is

swivelling out towards Vg max until the pressure drop across the

sensing orifice in the valve is restored. Δporifice = ppump – pactuator

Setting range for Δp: ______________________19 ... 40 bar Standard setting: _____________________________ 30 bar The stand-by pressure in zero stroke operation (sensing orifice plugged) is slightly above the Δp setting.

(1) The sensing orifice (control block) is not included in the pump supply. Characteristic DRS 350 50 max. 10 bar min max Displacement Operating pressure p B in bar Vg min Vg max Circuit diagram DRS R X T A (B) Vg min Vg max A1 R1 S (1)

Zero stroke operation

The standard pump unit is designed for intermittent constant pressure operation. Short-term operation at zero stroke (< 10 min.) is permissible up to a operating pressure pmax = 300 bar at a tank temperature of ≤ 50°C.

Note:

When using the DRS control a drain line is mandatory from the T port to tank to maintain thermal stability.

When ordering, state in clear text:

- Setting of the pressure control - Δp - setting of the load sensing function

(If there is no clear specification, pump will be delivered with standard setting, see above.)

(7)

EP - Electric Control with Proportional Solenoid

With the Electric control with proportional solenoid, the pump

displacement is adjusted proportionally to the solenoid current, resulting in a magnetic control force, acting directly onto the control spool that pilots the pump control piston.

EP2 - Starting position in unpressurised state at Vg min.

EP4 - Starting position in unpressurised state at Vg max.

Charactreristic EP 800 700 600 500 400 300 200 100 0 0,2 0,4 0,6 0,8 1,0

Vg min Displacement Vg max

C

ontrol current I in mA

EP2

EP4

Note:

For submerged in-tank installation when using the EP control, only the mineral hydraulic fluids can be used with the fluid temperature limited to 80°C.

To control the proportional solenoids the following electronic amplifier and controller are available (also as to the Internet under www.boschrexroth.com/mobile-electronic):

– BODAS controller RC (RE 95200)

and application software – Analog amplifier RA (RE 95230)

By using an proportional amplifier control of swivel time is also possible.

Technical data of solenoids

EP2 EP4

Sizes 55 107

Voltage 24VDC +20% 24VDC +20%

Control current

Start of control Vg min 200 mA Vg max 200 mA

End of control Vg max 600 mA Vg min 600 mA

Limiting current 0,77 A 0,68 A Nominal resistance (at 20°C) 22,7 Ω 24,2 Ω Dither frequency 100 Hz 100 Hz Duty cycle 100 % 100 % Type of protection IP 65 IP 54 Connector Hirschmann to DIN EN 175 301 - 803-A / ISO 4400 AMP- Junior Timer 2 pin Circuit diagram EP2 (Size 55) R A (B) Vg max Vg min A1 R1 S EP4 (Size 107) R A (B) Vg min Vg max A1 R1 S Note

The spring centering in the pilot control unit is not a safety device

Through contamination in the control unit – e.g. in hydraulic fluid, wear particles, or particles out of a system – the valve spool can get stuck in an undefined position. In this case, the pump flow does not follow the command inputs of the machi-ne operator anymore.

– Make sure that a proper emergency shut down function can bring the driven machine movements to a safe position immediately (e.g. stop).

– Maintain the specified cleanliness level 20/18/15 (<90°C) or 19/17/14 (>90°C) to ISO 4406.

(8)

Unit Dimensions, Size 55

Before finalizing your design, please request approved installation drawing. Dimensions in mm.

DRS Pressure control, with load sensing

1

A

1

R

R

1

T

X

S

A

T

1

A

X

R

Y

1

A

T

X

B

S

1

R

91 229 R120 17 10 *) 11 3 14 105 40 12 G3 /4 G1 118 27.5 27.5 -0.0 5 -0.03 ø8 0 ± 0.4 110 10 5 80 80 ø1 3 122 120 11 0 32 12°3 0' 76 18 0 39 9 15 156 130*) 214 267 242 232 *) center of gravity View Y conter-clockwise rotation View Y clockwise rotation

(9)

Unit Dimensions, Size 55

EP2 Electric control, with proportional solenoid

1

A

1

R

R

Y

1

R

1

A

B

S

1

R

A

1

A

S

13 1 276

Shaft end

E Splined shaft similar DIN ISO 14 8x32x35

Ports

A, B Service line ports (high pressure series) DIN ISO 228 G 3/4, 16 deep 330 Nm2)

S Suction port DIN ISO 228 G 1; 18 deep 480 Nm2)

T Case drain (only DRS) ISO 6149 M12x1,5; 12 deep 50 Nm2)

A1 Gauge port - high pressure 3) ISO 6149 M10x1; 8 deep 30 Nm2)

R1 Gauge port - suction pressure 3) ISO 6149 M10x1; 8 deep 30 Nm2)

R Air bleed 3) ISO 6149 M18x1,5 60 Nm2)

X Port for Δp control (load sensing) ISO 11926 7/16-20UNF-2B; 11,5 deep 40 Nm2) 1) centering bore according to DIN 332 (thread according to DIN13)

2) please observe the general notes for the max. tightening torques on page 15. 3) plugged 9.5 12 36.8 ø34.9 -0. 1 M1 2x1 .7 5 1) 2) 26.1 28 55 ø8. 1

groove for retaining ring 35x1.5 DIN 471

(1) (2)

Before finalizing your design, please request approved installation drawing. Dimensions in mm.

View Y

conter-clockwise rotation

View Y

clockwise rotation

Note:

The position of the plug can be changed by turning the solenoid body.

Note the following procedure: 1. Loosen the fastening nut (1)

2. Turn the magnet body (2) to the desired position 3. Tighten the fastening nut

Tightening torque of fastening nut: 5+1 Nm (width across flat 26, double hexagon DIN 3124)

(10)

Unit Dimensions, Size 80

DRS Pressure control, with load sensing

R120 103 18 248 12*) 128 14 105 40 12 G1 G1 1 /4 128 30 30 -0.0 5 -0.03 ø8 0 ± 0.4 117 10 5 80 80 ø1 3 128 126 11 6 36 12°3 0' 86 19 5 37 9 15 178 142*) 236 289 263 252 1

A

T

X

S

A

1

R

T

1

A

X

R

Y

1

A

T

X

B

S

1

R

1

R

*) center of gravity

Before finalizing your design, please request approved installation drawing. Dimensions in mm.

View Y

conter-clockwise rotation

View Y

(11)

Unit Dimensions, Size 80

Shaft end

E Splined shaft similar DIN ISO 14 8x32x35

Ports

A, B Service line ports (high pressure series) DIN ISO 228 G 1, 18 deep 480 Nm2)

S Suction port DIN ISO 228 G 1 1/4; 20 deep 720 Nm2)

T Case drain (only DRS) ISO 6149 M12x1,5; 12 deep 50 Nm2)

A1 Gauge port - high pressure 3) ISO 6149 M10x1; 8 deep 30 Nm2)

R1 Gauge port - suction pressure 3) ISO 6149 M10x1; 8 deep 30 Nm2)

R Air bleed 3) ISO 6149 M18x1,5; 60 Nm2)

X Port for Δp control (load sensing) ISO 11926 7/16-20UNF-2B; 11,5 deep 40 Nm2) 1) centering bore according to DIN 332 (thread according to DIN13)

2) please observe the general notes for the max. tightening torques on page 15. 3) plugged 9.5 12 36.8 ø34.9 -0. 1 M1 2x1 .7 5 1) 2) 26.1 28 55 ø8. 1

groove for retaining ring 35x1.5 DIN 471

Before finalizing your design, please request approved installation drawing. Dimensions in mm.

(12)

Unit Dimensions, Size 107

DRS Pressure control, with load sensing

19.5 259 11 0 172*) 14*) 264 91 20 6 -0.0 6 -0.03 ø8 0 15 307 282 43 9 250 132 191 40 134 ± 0.4 124 80 ø1 3 R120 13 8 10 5 80 G1 G1 1 /4 139 31.5 31.5 13 40 105 12°3 0' 124 14

T

S

A

1

A

X

1

R

T

T

R

X

B

S

1

A

X

Y

1

A

1

R

1

R

*) center of gravity

Before finalizing your design, please request approved installation drawing. Dimensions in mm.

View Y

conter-clockwise rotation

View Y

(13)

Unit Dimensions, Size 107

EP4 Electric control, with proportional solenoid

1

A

1

R

R

B

S

1

A

R

1

Y

S

A

1

R

A

1 17 8 306

Shaft end

E Splined shaft similar DIN ISO 14 8x32x35

Ports

A, B Service line ports (high pressure series) DIN ISO 228 G 1, 18 deep 480 Nm2)

S Suction port DIN ISO 228 G 1 1/4; 20 deep 720 Nm2)

T Case drain (only DRS) ISO 6149 M12x1,5; 12 deep 50 Nm2)

A1 Gauge port - high pressure 3) ISO 6149 M10x1; 8 deep 30 Nm2)

R1 Gauge port - suction pressure 3) ISO 6149 M10x1; 8 deep 30 Nm2)

R Air bleed 3) ISO 6149 M18x1,5; 60 Nm2)

X Port for Δp control (load sensing) ISO 11926 7/16-20UNF-2B; 11,5 deep 40 Nm2) 1) centering bore according to DIN 332 (thread according to DIN13)

2) please observe the general notes for the max. tightening torques on page 15. 3) plugged 9.5 12 36.8 ø34.9 -0. 1 M1 2x1 .7 5 1) 2) 26.1 28 55 ø8. 1

groove for retaining ring 35x1.5 DIN 471

Before finalizing your design, please request approved installation drawing. Dimensions in mm.

View Y

conter-clockwise rotation

View Y

(14)

General

During commissioning and operation, the axial piston unit must be filled with hydraulic fluid and air bled. This is also to be obser-ved following a relatively long standstill as the system can be drained through the hydraulic lines.

The case is connected to the inlet port S. A seperate case drain to tank is not required.

Exception: version with DRS control. When using the DRS control a drain line from port T to tank is mandatory to maintain thermal stability.

In all operating conditions, the suction and drain line must flow into the tank below the minimum fluid level. The minimum suction pressure at port S must not fall below 0,8 bar absolute.

Installation position

As to the examples mentioned below.

Installation below the tank (standard)

Pump below minimum fluid level in tank. Recommendation installation position: 1 and 2.

Installation above the tank

Pump above minimum fluid level in tank. - Note: - max. perm. suction height

hmax = 800 mm

- min. perm. suction pressure at port S



2

3

4

Installation

position Air bleed Filling Installation position Air bleed Filling

1 R S 3 R (L2) S (L2) 2 R1 S 4 R1 (L2) S (L2) T S R T S R1 A1 R T S R T S R1 A1 R T S R T S R1 A1 R T S R T S R1 A1 R T S R L2 T S R1 A1 R L2 T S R L2 T S R1 A1 R L2 T S R L2 T S R1 A1 R L2 T S R L2 T S R1 A1 R L2

Installation Notes

(15)

– The KVA pump is designed to be used in open circuits.

– Project planning, assembly and commissioning of the pump require the involvement of trained personnel. – The working and functional ports are only designed to accommodate hydraulic piping.

– There is a danger of burns from the pump and especially the solenoids during and shortly after operation. Suitable safety precautions, e.g. protective clothing plan.

– The characteristic curve may shift depending on the operating status (operating pressure, fluid temperature) of the pump. – Tightening torques:

- The tightening torques specified in this data sheet are maximum values and may not be exceeded (maximum value for screw thread). Manufacturer specifications for the max. permissible tightening torques of the used fittings must be observed! - For DIN 13 fastening screws we recommend checking the tightening torque individually according to VDI 2230 Edition 2003.

– The data and information contained herein must be adhered to.

General Notes

(16)

Bosch Rexroth AG Hydraulics

Product Segment Axial Piston Units Elchingen Plant Glockeraustraße 2 89275 Elchingen, Germany Phone +49 (0) 73 08 82-0 Facsimile +49 (0) 73 08 72 74 info.brm-ak@boschrexroth.de www.boschrexroth.com/axial-piston-pumps

© This document, as well as the data, specifications and other information set forth in it, are the exclusive property of Bosch Rexroth AG. It may not be reproduced or given to third parties without its consent.

The data specified above only serve to describe the product. No statements concerning a certain condition or suitability for a certain application can be derived from our information. The information given does not release the user from the obligation of own judgment and verification. It must be remembered that our products are subject to a natural process of wear and aging.

References

Related documents

This problem has a special form, and arises as an auxiliary problem in study of solutions’ properties of parametric Semi-infinite Programming (SIP) problems with finitely

coupling gauge dynamics below the scale of compactification, since by our assumption, the theory consists of neutral moduli fields and massless U(1) fields at the energy scale

To sum up, the visual appearance of the welded transmission lines mainly depends on the selected conductive yarn properties and textile materials for layers rather than the

Root-mean-square error (RMSE) of both Pearson (A) and SparCC (B) inferred correlations, as a function of the density of the underlying correlation network, as given by the

(___) Pledge or mortgage an interest in real property or right incident to real property as security to borrow money or pay, renew, or extend the time of payment of a debt of

navigation thereon, or for Barge Canal purposes, and be it further RESOLVED, that following publication of the notices of abandonment for the Property as required by Section 51 of

Students are not required to complete a formal master’s thesis, but will take a class (CIED 5013 or CIED 5273) that provides an introduction to education research and then design

Bio-medical sensors can also be useful to normally healthy users: for instance, a UV light sensor patch on the skin or integrated in a wearable device could trigger a smartphone app