Group 3 Gear Pumps. Technical Information. OpenCircuitGear MEMBER OF THE SAUER-DANFOSS GROUP

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1 Group 3 Gear Pumps OpenCircuitGear Technical Information

2 General Information History of revisions Table of revisions Date Page Changed Rev. 28, June 21 - First edition 24, Feb 211 1,2,11, 32 Covers to blue color, TurollaOCG brand name, Biofluids deleted. B Reference documents Literature reference for gear products Title Type Order number General luminum Gear Pumps and Motors L Group 1 Gear Pumps L Group 2 Gear Pumps L Group 1, 2 and 3 Gear Motors L11682 Hydraulic Fluids and Lubricants L Turolla OpenCircuitGear. ll rights reserved. TurollaOCG accepts no responsibility for possible errors in catalogs, brochures and other printed material. TurollaOCG reserves the right to alter its products without prior notice. This also applies to products already ordered provided that such alterations can be made without affecting agreed specifi cations. ll trademarks in this material are properties of their respective owners. Sauer-Danfoss, Turolla, Turolla OpenCircuitGear, TurollaOCG, OpenCircuitGear, Fast Lane and PLUS+1 are trademarks of the Sauer-Danfoss Group. 2 L February 211 Rev B

3 Contents General Information Overview... 4 Features... 4 Pump displacements... 4 Group 3 gear pumps` attributes... 4 SEP3NN... 5 SNP3NN... 5 Pump design... 5 Gear pump in circuit... 5 Technical data... 6 Determination of nominal pump sizes... 7 Based on SI units/based on US units... 7 Product Coding Model code... 8 System Requirements Pressure...1 Speed...1 Hydraulic fluids...11 Temperature and viscosity...11 Filtration...12 Filters...12 Selecting a filter...12 Reservoir...13 Line sizing...13 Pump drive...14 Pump drive data form...15 Pump life...16 Sound levels...17 Pump Performance Pump performance graphs...18 Product Options Shaft, flange, and port configurations...22 Mounting flanges...23 Shaft options...23 Port configurations...24 Porting...25 Dimensions SNP3NN 1F, 1D, 1B / SEP3NN 1B...26 SNP3NN 2F, 2D and 2B... SNP3NN 3FB, 3BB...28 SNP3NN 6DD, SNP3NN and SEP3NN 7S, 7G...3 L February 211 Rev B 3

4 General Information Overview The TurollaOCG Group 3 is a range of peak performance fixed-displacement gear pumps. Constructed of a high-strength extruded aluminum body with aluminum cover and flange, all pumps are pressure-balanced for exceptional efficiency. SNP3NN 7S SEP3NN 7S SEP3NN 7G SNP3NN 1B Features Group 3 gear pumps` attributes Wide range of displacements from 22 to 9 cm 3 /rev [from 1.34 to 5.49 in 3 /rev] Continuous pressure rating up to 25 bar [3625 psi] -1 Speeds up to 3 min (rpm) SE, DIN and European standard mounting flanges High quality case hardened steel gears Multiple pump configurations in combination with SNP1NN, SNP2NN and SNP3NN Pump displacements Quick reference chart for pump displacements vs. rated pressure Rated pressure (bar) SNP3NN SEP3NN Displacement (cm 3 /rev) 4 L February 211 Rev B

5 General Information Pump design SEP3NN The SEP3NN gear pump is available in a limited displacement range from 22. to 44.1 cm 3 /rev [from 1.34 to 2.69 in 3 /rev]. Suitable for applications where the pressure is lower than 21 bar [345 psi], the SEP3NN range is released into SE and European configurations. The overall length is reduced by 12 mm [.47 in] in respect of the SNP3NN. SNP3NN The SNP3NN is available in the full displacement range from 22. to 88.2 cm 3 /rev [from 1.34 to 5.38 in 3 /rev], and with higher pressure ratings than the SEP3NN. This is due to the pressure balance on each side of the gears obtained with pressure-balance plates made in antifriction alloy that contribute to high volumetric efficiency and maximum sealing as well. SNP3NN 1B (cut away) L February 211 Rev B 5

6 General Information Technical data Technical data for SNP3NN SNP3NN pump model Displacement Peak pressure Rated pressure cm 3 /rev [in 3 /rev] bar [psi] Frame size [1.35] [391] 25 [3625] Technical data for SEP3NN SEP3NN pump model Displacement Peak pressure Rated pressure cm 3 /rev [in 3 /rev] bar [psi] Frame size [1.35] 23 [335] 21 [345] 26.2 [1.6] 23 [335] 21 [345] 33.1 [2.2] 23 [335] 21 [345] 37.9 [2.32] 23 [335] 21 [345] 44.1 [2.69] 2 [291] 18 [261] Minimum speed min -1 (rpm) Maximum speed Weight 26.2 [1.6] [391] 25 [3625] Moment of inertia of rotating components Theoretical flow at maximum speed 33.1 [2.2] [391] 25 [3625] kg [lb] 37.9 [2.32] [391] 25 [3625] x 1-6 kg m 2 [x 1-6 lbf ft 2 ] l/min [US gal/min] 44.1 [2.69] [391] 25 [3625] 5.7 [12.57] 198 [4698] 66.3 [ [2.93] 25 [3625] 23 [335] 5.8 [12.79] 216 [5126] 78.6 [2.8].1 [3.36] 25 [3625] 23 [335] 63.4 [3.87] 23 [335] 21 [345] 6.1 [13.45] 246 [5873] 99.3 [26.2] 74.4 [4.54] 2 [291] 18 [261] 6.2 [13.67] [6981] [3.] 88.2 [5.38] 17 [2465] 15 [2175] Minimum speed min -1 (rpm) Maximum speed Weight Moment of inertia of rotating components Theoretical flow at maximum speed kg [lb] x 1-6 kg m 2 [x 1-6 lbf ft 2 ] l/min [US gal/min] 6.8 [15.] 198 [4698] 66.3 [17.5] 6.8 [15.] 216 [5126] 78.6 [2.8] 7.2 [15.8] 246 [5838] 99.3 [26.2] 7.3 [16.1] 267,2 [634] [3.] 7.5 [16.5] 294,2 [6891] [35.] 7.6 [16.8] 312,2 [748] [38.3] 7.8 [17.3] 342,3 [8123] [36.4] 8.1 [17.9] 378,3 [8977] [41.8] 8.5 [18.7] 426,4 [1118] 186 [49.1] 8.9 [19.6] 486,5 [11545] 22.5 [58.3] 6.4 [14.11] [748] [35.] C Caution The rated and peak pressure mentioned are for pumps with flanged ports only. When threaded ports are required a de-rated performance has to be considered. To verify the compliance of an high pressure application with a threaded ports pump apply to a TurollaOCG representative. 6 L February 211 Rev B

7 General Information Determination of nominal pump sizes Use these formulae to determine the nominal pump size for a specific application: Based on SI units Based on US units Output flow: Vg n η v Q = l/min 1 Vg n η v Q = [US gal/min] 231 Input torque: M = Vg p 2 π η m N m M = Vg p 2 π η m [lbf in] Input power: M n Q p P = = kw 9 6 η t M n Q p P = = [hp] η t Variables: SI units [US units] V g = Displacement per rev. cm 3 /rev [in 3 /rev] p HD = Outlet pressure bar [psi] p ND = Inlet pressure bar [psi] p = p HD p ND bar [psi] n = Speed min -1 (rpm) η v = Volumetric efficiency η m = Mechanical (torque) efficiency η t = Overall efficiency (η v η m ) L February 211 Rev B 7

8 Product Coding Model code B C D E F G H I J K L M N / / B Type SNP3NN SEP3NN Displacement Standard gear pump Medium pressure gear pump cm 3 /rev [1.35 in 3 /rev] cm 3 /rev [1.6 in 3 /rev] cm 3 /rev [2.2 in 3 /rev] cm 3 /rev [2.32 in 3 /rev] cm 3 /rev [2.69 in 3 /rev] cm 3 /rev [2.93 in 3 /rev].1 cm 3 /rev [3.36 in 3 /rev] cm 3 /rev [3.87 in 3 /rev] cm 3 /rev [4.54 in 3 /rev] cm 3 /rev [5.38 in 3 /rev] C D F Direction of rotation R Right hand (clockwise) L Left hand (counterclockwise) B For reversible motors Version N Standard gear pump Rear cover P1 Standard cover for pump E Mounting flange and drive gear Code Description (Type of flange type of drive gear prefered ports for configuration) SNP3NN SEP3NN 1F European four bolt flange Parallel shaft European flanged ports 1B European four bolt flange Tapered 1:8 shaft European flanged ports 1D European four bolt flange Splined 15T 12x1 shaft European flanged ports 2B European four bolts flange Tapered 1:8 shaft European flanged ports 2D European four bolts flange DIN splined shaft European flanged ports 2F European four bolts flange Parallel shaft European flanged ports 3BB European four bolts flange Tapered 1:8 shaft European flanged ports 3FB European four bolts flange Parallel shaft European flanged ports 6 German four bolts flange Tapered 1:5 shaft German standard ports 6DD German four bolts flange DIN Splined shaft German flanged ports 7G SE B flange Parallel shaft Vertical four bolt SE flanged ports 7S SE B flange SE splined shaft Vertical four bolt SE flanged ports Legend: Standard Optional Not vailable 8 L February 211 Rev B

9 Product Coding Model code (continued) B C D E F G H I J K L M N G Inlet port Code Description 2 8,5x22,23x47,63x ³/₈ -16UNC 3 25x26,19x52,37x ³/₈ -16UNC 4 31x3,18x58,72x 7/ ₁₆ -14UNC 5 37,5/x35,7x69,85x ½ -13UNC B7 2x4xM6 B 18xx BB xx BC 36/xx C3 13,5x3xM6 C7 2x4x C x51xm1 CD 36x62xM1 E6 1 1/ ₁₆-12UN E8 1 5/ ₁₆-12UN E9 1 5/₈-12UN E 1 ⁷/ ₈-12UN F5 ¾ GS F6 1 GS F7 1 ¼ GS SE flanged port Flanged port with thd holes in X pattern Flanged port with thd holes in + pattern Thd SE O-ring boss port Threaded GS (BSPP) H Outlet port For code letters and descriptions see the table above. I Port position and variant body NN Standard gear pump from catalogue L Set valve NNN V** No valve Integral RV-pressure setting. Pump speed for relief valve setting J Sealing N Standard Buna seal Without shaft seal B VITON seals M Marking N Z Standard marking Standard marking + customer code Without marking K Screws N Standard screws Galvanized screws+nuts-washers B DCROMET/GEOMET screws N Mark position N Standard marking position Mark on the bottom reffering to drive gear L February 211 Rev B 9

10 System Requirements Pressure The inlet vacuum must be controlled in order to realize expected pump life and performance. The system design must meet inlet pressure requirements during all modes of operation. Expect lower inlet pressures during cold start. It should improve quickly as the fluid warms. Peak pressure is the highest intermittent pressure allowed. The relief valve overshoot (reaction time) determines peak pressure. It is assumed to occur for less than 1 ms. The illustration to the right shows peak pressure in relation to rated pressure and reaction time (1 ms maximum). Rated pressure is the average, regularly occurring, operating pressure that should yield satisfactory product life. The maximum machine load demand determines rated pressure. For all systems, the load should move below this pressure. Inlet pressure Max. continuous vacuum.8 [23.6] bar abs. Max. intermittent vacuum.6 [17.7] [in. Hg] Max. pressure 3. [88.5] Time versus pressure Pressure Peak pressure Rated pressure Reaction time (1 ms max) Time System pressure is the differential of pressure between the outlet and inlet ports. It is a dominant operating variable affecting hydraulic unit life. High system pressure, resulting from high load, reduces expected life. System pressure must remain at, or below, rated pressure during normal operation to achieve expected life. Speed Maximum speed is the limit recommended by TurollaOCG for a particular gear pump when operating at rated pressure. It is the highest speed at which normal life can be expected. Speed versus pressure Rated The lower limit of operating speed is the minimum speed. It is the lowest speed at which normal life can be expected. The minimum speed increases as operating pressure increases. When operating under higher pressures, a higher minimum speed must be maintained, as illustrated to the right. Pressure P 1 N1 N 2 Speed Where: N 1 = Minimum speed at 1 bar N 2 = Minimum speed at 18 bar Operating envelope Max 1 L February 211 Rev B

11 System Requirements Hydraulic fluids Ratings and data for SNP3NN and SEP3NN gear pumps are based on operating with premium hydraulic fluids containing oxidation, rust, and foam inhibitors. These fluids must possess good thermal and hydrolytic stability to prevent wear, erosion, and corrosion of internal components. They include: Hydraulic fluids following DIN 51524, part 2 (HLP) and part 3 (HVLP) specifications PI CD engine oils conforming to SE J183 M2C33F or G automatic transmission fluids Certain agricultural tractor fluids Use only clean fluid in the pump and hydraulic circuit. C Caution Never mix hydraulic fluids. Please see TurollaOCG publication Hydraulic Fluids and Lubricants Technical Information, L for more information. Temperature and Viscosity Temperature and viscosity requirements must be concurrently satisfied. Use petroleum / mineral-based fluids. High temperature limits apply at the inlet port to the pump. The pump should run at or below the maximum continuous temperature. The peak temperature is based on material properties. Don t exceed it. Cold oil, generally, doesn t affect the durability of pump components. It may affect the ability of oil to flow and transmit power. For this reason, keep the temperature at 16 C [6 F] above the pour point of the hydraulic fluid. Minimum (cold start) temperature relates to the physical properties of component materials. Minimum viscosity occurs only during brief occasions of maximum ambient temperature and severe duty cycle operation. You will encounter maximum viscosity only at cold start. During this condition, limit speeds until the system warms up. Size heat exchangers to keep the fluid within these limits. Test regularly to verify that these temperatures and viscosity limits aren t exceeded. For maximum unit efficiency and bearing life, keep the fluid viscosity in the recommended viscosity range. Fluid viscosity Maximum (cold start) 1 [46] mm 2 /s Recommended range 12-6 [66-29] [SUS] Minimum 1 [6] Temperature Minimum (cold start) -2 [-4] C Maximum continuous 8 [176] [ F] Peak (intermittent) 9 [194] L February 211 Rev B 11

12 System Requirements Filtration Filters Use a filter that conforms to Class 22/18/13 of ISO 446 (or better). It may be on the pump outlet (pressure filtration), inlet (suction filtration), or reservoir return (return-line filtration). Selecting a filter When selecting a filter, please consider: contaminant ingression rate (determined by factors such as the number of actuators used in the system) generation of contaminants in the system required fluid cleanliness desired maintenance interval filtration requirements of other system components Measure filter efficiency with a Beta ratio (β X ). For: suction filtration, with controlled reservoir ingression, use a β = 75 filter return or pressure filtration, use a pressure filtration with an efficiency of β 1 = 75. β x ratio is a measure of filter efficiency defined by ISO It is the ratio of the number of particles greater than a given diameter ( X in microns) upstream of the filter to the number of these particles downstream of the filter. Fluid cleanliness level and β x ratio Fluid cleanliness level (per ISO 446) Class 22/18/13 or better β x ratio (suction filtration) β = 75 and β 1 = 2 β x ratio (pressure or return filtration) β 1 = 75 Recommended inlet screen size µm [.4-.5 in] The filtration requirements for each system are unique. Evaluate filtration system capacity by monitoring and testing prototypes. 12 L February 211 Rev B

13 System Requirements Reservoir The reservoir provides clean fluid, dissipates heat, removes entrained air, and allows for fluid volume changes associated with fluid expansion and cylinder differential volumes. correctly sized reservoir accommodates maximum volume changes during all system operating modes. It promotes deaeration of the fluid as it passes through, and accommodates a fluid dwell-time between 6 and 18 seconds, allowing entrained air to escape. Minimum reservoir capacity depends on the volume required to cool and hold the oil from all retracted cylinders, allowing for expansion due to temperature changes. fluid volume of 1 to 3 times the pump output flow (per minute) is satisfactory. The minimum reservoir capacity is 125% of the fluid volume. Install the suction line above the bottom of the reservoir to take advantage of gravity separation and prevent large foreign particles from entering the line. Cover the line with a micron screen. The pump should be below the lowest expected fluid level. Put the return-line below the lowest expected fluid level to allow discharge into the reservoir for maximum dwell and efficient deaeration. baffle (or baffles) between the return and suction lines promotes deaeration and reduces fluid surges. Line sizing Choose pipe sizes that accommodate minimum fluid velocity to reduce system noise, pressure drops, and overheating. This maximizes system life and performance. Design inlet piping that maintains continuous pump inlet pressure above.8 bar absolute during normal operation. The line velocity should not exceed the values in this table: Maximum line velocity Inlet 2.5 [8.2] Outlet m/s [ft/sec] 5. [16.4] Return 3. [9.8] Most systems use hydraulic oil containing 1% dissolved air by volume. Under high inlet vacuum conditions the oil releases bubbles. They collapse when subjected to pressure, resulting in cavitation, causing adjacent metal surfaces to erode. Over-aeration is the result of air leaks on the inlet side of the pump, and flow-line restrictions. These include inadequate pipe sizes, sharp bends, or elbow fittings, causing a reduction of flow line cross sectional area. This problem will not occur if inlet vacuum and rated speed requirements are maintained, and reservoir size and location are adequate. L February 211 Rev B 13

14 System Requirements Pump drive Shaft options for Group 3 gear pumps include tapered, splined, or parallel shafts. They are suitable for a wide range of direct and indirect drive applications for radial and thrust loads. Plug-in drives, acceptable only with a splined shaft, can impose severe radial loads when the mating spline is rigidly supported. Increasing spline clearance does not alleviate this condition. Pilot cavity Mating spline Use plug-in drives if the concentricity between the mating spline and pilot diameter is within.1 mm [.4 in]. Lubricate the drive by flooding it with oil. 3-piece coupling minimizes radial or thrust shaft loads. Ø.1 [.4] P11 2E CCaution In order to avoid spline shaft damages it is recommended to use carburised and hardened steel couplings with 8-82 HR surface hardness. llowable radial shaft loads are a function of the load position, load orientation, and operating pressure of the hydraulic pump. ll external shaft loads have an effect on bearing life, and may affect pump performance. In applications where external shaft loads can t be avoided, minimize the impact on the pump by optimizing the orientation and magnitude of the load. Don t use splined shafts for belt or gear drive applications. spring-loaded belt tension-device is recommended for belt drive applications to avoid excessive tension. void thrust loads in either direction. Contact TurollaOCG if continuously applied external radial or thrust loads occur. 14 L February 211 Rev B

15 System Requirements Pump drive data form Photocopy this page and fax the complete form to your TurollaOCG representative for an assistance in applying pumps with belt or gear drive. This illustration shows a pump with counterclockwise orientation: Optimal radial load position 9 o 9 o α a Inlet port 18 o o o 18 o Inlet port o o P a a dw dw pplication data Item Value Unit Pump displacement cm 3 /rev [in 3 /rev] Rated system pressure Relief valve setting bar psi Pump shaft rotation left right Pump minimum speed min -1 (rpm) Pump maximum speed Drive gear helix angle (gear drive only) degree Belt type (gear drive only) V notch Belt tension (gear drive only) P N lbf ngular orientation of gear or belt to inlet port α degree Pitch diameter of gear or pulley d w mm in Distance from flange to center of gear or pulley a L February 211 Rev B 15

16 System Requirements Pump life Pump life is a function of speed, system pressure, and other system parameters (such as fluid quality and cleanliness). ll TurollaOCG gear pumps use hydrodynamic journal bearings that have an oil film maintained between the gear / shaft and bearing surfaces at all times. If the oil film is sufficiently sustained through proper system maintenance and operating within recommended limits, long life can be expected. B 1 life expectancy number is generally associated with rolling element bearings. It does not exist for hydrodynamic bearings. High pressure, resulting from high loads, impacts pump life. When submitting an application for review, provide machine duty cycle data that includes percentages of time at various loads and speeds. We strongly recommend a prototype testing program to verify operating parameters and their impact on life expectancy before finalizing any system design. 16 L February 211 Rev B

17 System Requirements Sound levels Fluid power systems are inherent generators of noise. s with many high power density devices, noise is an unwanted side affect. However, there are many techniques available to minimize noise from fluid power systems. To apply these methods effectively, it is necessary to understand how the noise is generated and how it reaches the listener. The noise energy can be transmitted away from its source as either fluid borne noise (pressure ripple) or as structure borne noise. Pressure ripple is the result of the number of pumping elements (gear teeth) delivering oil to the outlet and the pump s ability to gradually change the volume of each pumping element from low to high pressure. In addition, the pressure ripple is affected by the compressibility of the oil as each pumping element discharges into the outlet of the pump. Pressure pulsations will travel along the hydraulic lines at the speed of sound (about 14 m/s in oil) until affected by a change in the system such as an elbow fitting. Thus the pressure pulsation amplitude varies with overall line length and position. Structure borne noise may be transmitted wherever the pump casing is connected to the rest of the system. The manner in which one circuit component responds to excitation depends on its size, form, and manner in which it is mounted or supported. Because of this excitation, a system line may actually have a greater noise level than the pump. To reduce this excitation, use flexible hoses in place of steel plumbing. If steel plumbing must be used, clamping of lines is recommended. To minimize other structure borne noise, use flexible (rubber) mounts. The accompanying graph shows typical sound pressure levels for SNP3NN pumps (with SE flange, and spline shaft in plug in drive) measured in db () at 1 m [3.28 ft] from the unit in a semi-anechoic chamber. nechoic levels can be estimated by subtracting 3 db () from these values. Contact your TurollaOCG representative for assistance with system noise control. Sound levels graph 8 Sound pressure level (db() at 1m [3.3ft]) rpm, 175 bar [2538 psi] 3 rpm, 175 bar [2538 psi] 18 rpm, 25 bar [3626 psi] 3 rpm, 25 bar [3626 psi] Displacement (cc/rev) L February 211 Rev B 17

18 Pump Performance Pump performance graphs The graphs on the next few pages provide typical output flow and input power for Group 3 pumps at various working pressures. Data were taken using ISO VG46 petroleum /mineral based fluid at 5 C [122 F] (viscosity = 28 mm2/s [132 SUS]). SNP3NN/22 pump performance graph 7 [18.5] SNP3NN/26 pump performance graph 8 [21.1] 6 [15.8] SNP3NN/22 7 [18.5] SNP3NN/26 Flow l/min [US gal/min] 5 [13.2] 4 [1.6] 3 [7.9] 7 bar 25 bar 25 bar Power kw [hp] 3 [4.2] Flow l/min [US gal/min] 6 [15.8] 5 [13.2] 4 [1.6] 3 [7.9] 7 bar 25 bar 25 bar Power kw [hp] 4 [53.6] 3 [4.2] 2 1 [5.3] [2.6] 15 bar 1 bar 2 [16.8] 1 [13.4] 2 1 [5.3] [2.6] 15 bar 1 bar 2 [16.8] 1 [13.4] Speed min -1 (rpm) Speed min -1 (rpm) SNP3NN/33 pump performance graph SNP3NN/38 pump performance graph 11 [29.] 1 [26.4] 9 [23.8] SNP3NN/33 7 bar 11 [29.] 1 [26.4] SNP3NN/38 7 bar Flow l/min [US gal/min] 8 [21.1] 7 [18.5] 6 [15.8] 5 [13.2] 4 [1.6] 25 bar 25 bar Power kw [hp] 5 [67.1] 4 [53.6] Flow l/min [US gal/min] 9 [23.8] 8 [21.1] 7 [18.5] 6 [15.8] 5 [13.2] 4 [1.6] 25 bar 25 bar Power kw [hp] 6 [8.5] 5 [67.1] 4 [53.6] 3 2 [7.9] [5.3] 15 bar 1 bar 3 [4.2] 2 [16.8] 3 [7.9] 2 [5.3] 15 bar 1 bar 3 [4.2] 2 [16.8] 1 [2.6] 1 [13.4] 1 [2.6] 1 [13.4] Speed min -1 (rpm) Speed -1 min (rpm) 18 L February 211 Rev B

19 Pump Performance Pump performance graphs (continued) SNP3NN/44 pump performance graph 14 [37.] SNP3NN/48 pump performance graph 14 [37.] 13 [34.3] 12 [31.7] SNP3NN/44 7 bar 13 [34.3] 12 [31.7] SNP3NN/48 7 bar 11 [29.] 1 [26.4] 25 bar 11 [29.] 1 [26.4] 25 bar Flow l/min [US gal/min] 9 [23.8] 8 [21.1] 7 [18.5] 6 [15.8] 5 [13.2] 25 bar Power kw [hp] 6 [8.5] 5 [67.1] Flow l/min [US gal/min] 9 [23.8] 8 [21.1] 7 [18.5] 6 [15.8] 5 [13.2] 25 bar Power kw [hp] 6 [8.5] 5 [67.1] 4 [1.6] 3 [7.9] 2 [5.3] 15 bar 1 bar 4 [53.6] 3 [4.2] 2 [16.8] 4 [1.6] 3 [7.9] 2 [5.3] 15 bar 1 bar 4 [53.6] 3 [4.2] 2 [16.8] 1 [2.6] 1 [13.4] 1 [2.6] 1 [13.4] Speed min -1 (rpm) Speed min -1 (rpm) SNP3NN/ pump performance graph 15 [39.6] SNP3NN/63 pump performance graph 16 [42.3] 14 [37.] 13 [34.3] SNP3NN/ 14 [37.] SNP3NN/63 Flow l/min [US gal/min] 12 [31.7] 11 [29.] 1 [26.4] 9 [23.8] 8 [21.1] 7 [18.5] 6 [15.8] 5 [13.2] 4 [1.6] 3 [7.9] 2 [5.3] 7 bar 23 bar 15 bar 23 bar 1 bar Power kw [hp] 6 [8.5] 5 [67.1] 4 [53.6] 3 [4.2] 2 [16.8] Flow l/min [US gal/min] 12 [31.7] 1 [26.4] 8 [21.1] 6 [15.8] 4 [1.6] 2 [5.3] 7 bar 21 bar 15 bar 21 bar 1 bar Power kw [hp] 6 [8.5] 4 [53.6] 2 [16.8] 1 [2.6] 1 [13.4] Speed min -1 (rpm) Speed min -1 (rpm) L February 211 Rev B 19

20 Pump Performance Pump performance graphs (continued) SNP3NN/75 pump performance graph 2 [52.8] SNP3NN/9 pump performance graph 18 [47.6] SNP3NN/75 22 [58.1] SNP3NN/9 Flow l/min [US gal/min] Flow l/min [US gal/min] 16 [42.3] 14 [37.] 12 [31.7] 1 [26.4] 8 [21.1] 8 [17.3] 6 [15.8] 4 [1.6] 7 bar 18 bar 18 bar 1 bar 21 bar 15 bar 7 bar 6 [8.5] 4 [53.6] 2 [5.3] 2 [16.8] Speed min -1 (r pm) SEP3NN/22 pump performance graph 7 [18.5] SEP3NN/22 6 [15.8] 5 [13.2] 4 [1.6] 3 [7.9] 3 [4.2] Power kw [hp] Power kw [hp] Flow l/min [US gal/min] Flow l/min [US gal/min] 2 [52.8] 18 [47.6] 16 [42.3] 14 [37.] 12 [16.9] 12 [31.7] 1 [134.1] 1 [26.4] 8 [21.1] 6 [15.8] 14 bar 1 bar 14 bar 4 [53.6] 4 [1.6] 2 [5.3] 2 [16.8] Speed min -1 (r pm) SEP3NN/26 pump performance graph 8 [21.1] SEP3NN/26 7 [18.5] 6 [15.8] 5 [13.2] 4 [1.6] 7 bar 21 bar 7 bar 8 [17.3] 6 [8.5] 3 [7.9] 3 [4.2] Power kw [hp] Power kw [hp] 2 1 [5.3] [2.6] 21 bar 15 bar 1 bar 2 [16.8] 1 [13.4] 2 1 [5.3] [2.6] 21 bar 15 bar 1 bar 2 [16.8] 1 [13.4] Speed min -1 (r pm) Speed min -1 (r pm) 2 L February 211 Rev B

21 Pump Performance Pump performance graphs (continued) SEP3NN/33 pump performance graph SEP3NN/38 pump performance graph 1 [26.4] 9 [23.8] 8 [21.1] 7 [18.5] SEP3NN/33 7 bar 1 [26.4] 9 [23.8] 8 [21.1] SEP3NN/38 7 bar Flow l/min [US gal/min] 6 [15.8] 5 [13.2] 4 [1.6] 21 bar Power kw [hp] Flow l/min [US gal/min] 7 [18.5] 6 [15.8] 5 [13.2] 4 [1.6] 21 bar Power kw [hp] 4 [53.6] 3 2 [7.9] [5.3] 21 bar 15 bar 1 bar 3 [4.2] 2 [16.8] 3 2 [7.9] [5.3] 21 bar 15 bar 1 bar 3 [4.2] 2 [16.8] 1 [2.6] 1 [13.4] 1 [2.6] 1 [13.4] Speed min -1 (rpm) Speed min -1 (rpm) SEP3NN/44 pump performance graph 12 [31.7] 11 [29.] 1 [26.4] SEP3NN/44 9 [23.8] Flow l/min [US gal/min] 8 [21.1] 7 [18.5] 6 [15.8] 5 [13.2] [1.6] 4 [7.9] 3 [5.3] 2 [2.6] 1 7 bar 18 bar 18 bar 15 bar 1 bar Power kw [hp] 4 [53.6] 3 [4.2] 2 [16.8] 1 [13.4] Speed min -1 (rpm) L February 211 Rev B 21

22 Product Options Shaft, flange, and port configurations Pump Code Flange Shaft Port SEP3NN SNP3NN 1B pilot Ø 5.8 mm [2. in] European 1, 4-bolt 1:8 tapered European flanged port + pattern SNP3NN 2B pilot Ø 5.8 mm [2. in] European 2, 4-bolt 1:8 tapered European flanged port + pattern SNP3NN 3BB pilot Ø 6.3 mm [2.374 in] European 3, 4-bolt 1:8 tapered European flanged port + pattern SNP3NN 6 pilot Ø 15 mm [4.133 in] German, 4-bolt 1:5 tapered German std ports port X pattern SEP3NN SNP3NN 1F pilot Ø 5.8 mm [2. in] European 1, 4-bolt Ø 2 mm [.787 in] parallel European flanged port + pattern SNP3NN 2F pilot Ø 5.8 mm [2. in] European 2, 4-bolt Ø 2 mm [.787 in] parallel European flanged port + pattern SNP3NN 3FB pilot Ø 6.3 mm [2.374 in] European 3, 4-bolt Ø 22 mm [.866 in] parallel European flanged port + pattern SEP3NN SNP3NN 7G pilot Ø 11.6 mm [4. in] SE B, 2-bolt Ø mm [.875 in] parallel Vertical four bolt flanged port SNP3NN 1D pilot Ø 5.8 mm [2. in] European 1, 4-bolt Splined shaft 13T - m 1.6 DIN 5482-B22x19 European flanged port + pattern SNP3NN 2D pilot Ø 5.8 mm [2. in] European 2, 4-bolt Splined shaft 13T - m 1.6 DIN 5482-B22x19 European flanged port + pattern SNP3NN 6DD pilot Ø 15 mm [4. in] German, 4-bolt Splined shaft 15T - m 1.75 DIN 5482-B28x25 German std ports port X pattern SEP3NN SNP3NN 7S pilot Ø 11.6 mm [4. in] SE B, 2-bolt Splined shaft SE J498 13T - 16/32DP Vertical four bolt flanged port 22 L February 211 Rev B

23 Product Options Mounting flanges TurollaOCG offers many types of industry standard mounting flanges. This table shows order codes for each available mounting flange and its intended use: Flange availability B C D E F G H I J K L M N / / Code Description 1 2 European 5.8 mm [2. in] 4-bolt 3 European 6.3 mm [2.374 in] 4-bolt 6 German 15 mm [4.134 in] 4-bolt 7 SE B 2-bolt Shaft options Direction is viewed facing the shaft. Group 3 pumps are available with a variety of splined, parallel, and tapered shaft ends. Not all shaft styles are available with all flange styles. Shaft availability and nominal torque capability B C D E F G H I J K L M N / / Shaft Mounting flange code with maximum torque in Nm [lb in] Code Description Taper 1:5 3 [26] B Taper 1:8 35 [397] 35 [397] BB Taper 1:8 5 [4425] D Spline 13T DIN 5482-B22X19 29 [2566] 29 [2566] DD Spline 13T DIN 5482-B28X25 45 [3982] S SE spline 13T 16/32p [2389] F Parallel ø2 mm 21 [1858] 21 [1858] FB Parallel ø mm 3 [26] G Parallel ø mm 23 [235] TurollaOCG recommends mating splines conform to SE J498 or DIN Turolla OCG external SE splines have a flat root side fit with circular tooth thickness reduced by.1 mm [.5 in] in respect to class 1 fit. Dimensions are modified to assure a clearance fit with the mating spline. C Caution Shaft torque capability may limit allowable pressure. Torque ratings assume no external radial loading. pplied torque must not exceed these limits, regardless of stated pressure parameters. Maximum torque ratings are based on shaft torsional fatigue strength. L February 211 Rev B 23

24 Product Options Port configurations Various port configurations are available on Group 3 pumps. They include: European standard flanged ports German standard flanged ports Gas threaded ports (BSPP) O-Ring boss (following SE J1926/1 [ISO ] UNF threads, standard) table of dimensions is on the next page. vailable port configurations B C D E F G H I J K L M N / / G Code B7 B BB BC C3 C7 C CD E6 E8 E9 E F5 F6 F7 Inlet port Description 8,5x22,23x47,63x ³/₈ -16UNC 25x26,19x52,37x ³/₈ -16UNC 31x3,18x58,72x 7/ ₁₆ -14UNC 37,5/x35,7x69,85x ½ -13UNC 2x4xM6 18xx xx 36/xx 13,5x3xM6 2x4x x51xm1 36x62xM1 1 1/ ₁₆-12UN 1 5/ ₁₆-12UN 1 5/₈-12UN 1 ⁷/ ₈-12UN ¾ GS 1 GS 1 ¼ GS SE flanged port Flanged port with thd holes in X pattern Flanged port with thd holes in + pattern Thd SE O-ring boss port Threaded GS (BSPP) H Outlet port For code letters and descriptions see the table above. 24 L February 211 Rev B

25 Product Options Porting B C E F a 45 o d Ports dimensions b c (4 holes min. full thd. 2 [.787] deep) x y z (4 holes min. full thd. 12 [.472] deep) h g i (4 holes min. full thd. 12 [.472] deep) Port type B C E F Dimensions a b d c x y z g h i e f Type (displacement) Inlet Outlet Inlet Outlet Inlet Outlet Inlet Outlet Inlet Outlet Inlet Outlet Inlet Outlet Inlet Outlet Inlet Outlet Inlet Outlet 25.4 [1.] 19.1 [.752] 25.4 [1.] 19.1 [.752] 31.8 [1.252] 25.4 [1.] 31.8 [1.252] 25.4 [1.] 31.8 [1.252] 25.4 [1.] 31.8 [1.252] 25.4 [1.] 38.1 [1.5] 31.8 [1.252] 38.1 [1.5] 31.8 [1.252] 38.1 [1.5] 31.8 [1.252] 38.1 [1.5] 31.8 [1.252] [1.31] [.875] [1.31] [.875] 3.18 [1.188] [1.31] 3.18 [1.188] [1.31] 3.18 [1.188] [1.31] 3.18 [1.188] [1.31] [1.46] 3.18 [1.188] [1.46] 3.18 [1.188] [1.46] 3.18 [1.188] [1.46] 3.18 [1.188] [2.62] [1.875] [2.62] [1.875] [2.312] [2.62] [2.312] [2.62] [2.312] [2.62] [2.312] [2.62] [2.75] [2.312] [2.75] [2.312] [2.75] [2.312] [2.75] [2.312] 3/8 16UNC 2B 3/8 16UNC 2B 3/8 16UNC 2B 3/8 16UNC 2B 7/16 14UNC 2B 3/8 16UNC 2B 7/16 14UNC 2B 3/8 16UNC 2B 7/16 14UNC 2B 3/8 16UNC 2B 7/16 14UNC 2B 3/8 16UNC 2B ½ 13UNC 2B 7/16 14UNC 2B ½ 13UNC 2B 7/16 14UNC 2B ½ 13UNC 2B 7/16 14UNC 2B ½ 13UNC 2B 7/16 14UNC 2B [1.63] 18 [.79] [1.63] 18 [.79] [1.63] 18 [.79] [1.63] 18 [.79] [1.63] 18 [.79] [1.63] 18 [.79] [1.63] 18 [.79] 36 [1.417] [1.63] 36 [1.417] [1.63] 36 [1.417] [1.63] 4 [1.575] 4 [1.575] 4 [1.575] 4 [1.575] 51 [2.8] 4 [1.575] 51 [2.8] 4 [1.575] 51 [2.8] 51 [2.8] 51 [2.8] 51 [2.8] 51 [2.8] 51 [2.8] 62 [2.441] 51 [2.8] 62 [2.441] 51 [2.8] 62 [2.441] 51 [2.8] e 2 [.787] 2 [.787] 2 [.787] 2 [.787] [1.63] 2 [.787] [1.63] 2 [.787] [1.63] [1.63] [1.63] [1.63] [1.63] [1.63] 36 [1.417] [1.63] 36 [1.417] [1.63] 36 [1.417] [1.63] f 15/16 12UN 2B ¾ Gas (BSPP) 11/16 12UN 2B ¾ Gas (BSPP) 15/16 12UN 2B ¾ Gas (BSPP) 11/16 12UN 2B ¾ Gas (BSPP) M1 15/8 12UN 2B 1 Gas (BSPP) 15/16 12UN 2B ¾ Gas (BSPP) M1 15/8 12UN 2B 1 Gas (BSPP) 15/16 12UN 2B ¾ Gas (BSPP) M1 15/8 12UN 2B 1 Gas (BSPP) M1 15/16 12UN 2B 1 Gas (BSPP) M1 15/8 12UN 2B 1 Gas (BSPP) M1 15/16 12UN 2B 1 Gas (BSPP) M1 17/8 12UN 2B 1 Gas (BSPP) M1 15/8 12UN 2B 1 Gas (BSPP) M1 17/8 12UN 2B 1¼ Gas (BSPP) M1 15/8 12UN 2B 1 Gas (BSPP) M1 17/8 12UN 2B 1¼ Gas (BSPP) M1 15/8 12UN 2B 1 Gas (BSPP) M1 17/8 12UN 2B 1¼ Gas (BSPP) M1 15/8 12UN 2B 1 Gas (BSPP) L February 211 Rev B 25

26 Dimensions SNP3NN 1F, 1D, 1B / SEP3NN 1B The drawing shows the SNP3NN standard porting for 1F, 1D and 1B. The configurations 1F and 1B are available for the SEP3NN. mm 1F 1D 1B [in] 4 [1.574] Ø [ ] SNP3NN 1F, 1B, 1D and SEP3NN 1F, 1B dimensions Dimension Inlet Outlet 46 [1.118] 6 [.236] Distance from front flange to shoulder (full thd 18 [.78] deep) [ ] [ ] -.2 Frame size B 34 [1.338] Ø [ ] 63 [2.48] [5.216] 5 [.196] Distance from front flange to shoulder 24 [.944] Spline: B22x19 DIN 5482 (Profile offset -.1 [.24]) 64.5 [2.539] [5.334] 67 [2.637] 14.5 [5.531] 46.5 [1.83] 68.8 [2.78] 144 [5.669] 2 [.787] 14.5 [.571] 24 8 [.314] -.3 Ø [ ] Ø 22 [.866] M14x1.5-6g X ±.5 [.874 ±.2] 71 [2.795] [5.846] 72.5 [2.854] [5.964] 75 [2.952] [6.161] 78 [3.7] [6.397] C 2 [.787] [1.63] 36 [1.417] D 4 [1.575] 51 [2.7] 62 [2.441] E M1 c 2 [.787] [1.63] d 4 [1.575] 51 [2.1] e M1 [.944] 5 [.196] 1:8 B B B max 22 [.866] (full thd 12 [.472] deep) M1 (full thd 17 [.669] deep) < 4: ±.2 [.8] D/d > 4: ±.25 [.1] [ ] B - B 11.5 ±.75 [±.3] E/e [.453 ] C/c (128.1 [5.43]) 85.2 [3.354] 42.9 [1.689] Ø.75 X 115 ±.25 [4.5 ±.1] [ ] 98.4 [3.874] [4.783] max 82 [3.228] 17.5 [6.712] (54.3 [2.137]) 148 [ 5.826] max (96.2 [3.787]) 15.5 [5.925] max 87 [3.425] 18.5 [7.16] The SEP3NN overall length is 12 mm [.472 in] less than the SNP3NN for the whole range of displacements (22.1 to 44.1 cm 3 /rev [1.35 to 2.69 in 3 /rev]). Model code examples and maximum shaft torque Flange/drive gear Model code example Maximum shaft torque 1D SNP3NN/75LN1DP1CDCNNNN/NNNNN 29 N m [2566 lb in] 1F SNP3NN/33RN1FP1CC7NNNN/NNNNN 21 N m [1858 lb in] 1B SNP3NN/22RN1BP1C7C7NNNN/NNNNN 35 N m [397 lb in] For further details on ordering, see Model Code, pages L February 211 Rev B

27 X OpenCircuitGear Dimensions SNP3NN 2F, 2D and 2B This drawing shows the standard porting for 2F, 2D and 2B. 2F 2D 46.5 [1.83] 2B B max mm [in] 2 [.787] ±.75 [±.3] 4 [1.574] 46 [1.118] 6 [.236] Distance from front flange to shoulder 34 [1.338] 5 [.196] Distance from front flange to shoulder 14.5 [.571] 24 8 [.314] -.3 Ø [ ] Ø 22 [.866] M14x1.5-6g [.944] 5 [.196] B 22 [.866] 45 [1.77] [4.9] max 98.4 [3.87] 58 [2.28] max Ø [ ] (full thd 18 [.78] deep) [ ] [ ] -.2 Ø [ ] 24 [.944] Spline: B22x19 DIN 5482 (Profile offset -.1 [.24]) Nut and washer supplied with pump Recommended tightening torque: Nm ±.5 [.874 ±.2] 1:8 B (full thd 12 [.472] deep) M1 (full thd 17 [.669] deep) < 4: ±.2 [.8] D/d > 4: ±.25 [.1] [ ] B - B 11.5 E/e [.453 ] C/c (137 [5.39]) 92 [3.62] ±.75 [1.75 ±.3] Ø.75 [.3] X 115 ±.25 [4.5 ±.1] body width [ ] 148 [ 5.826] max 15 [4.13] max 163 [6.42] max SNP3NN 2F, 2D and 2B dimensions Dimension Inlet Outlet Frame size B 63 [2.48] [5.216] 64.5 [2.539] [5.334] 67 [2.637] 14.5 [5.531] 68.8 [2.78] 144 [5.669] 71 [2.795] [5.846] 72.5 [2.854] [5.964] 75 [2.952] [6.161] 78 [3.7] [6.397] C 2 [.787] [1.63] 36 [1.417] D 4 [1.575] 51 [2.7] 62 [2.441] E M1 c 2 [.787] [1.63] d 4 [1.575] 51 [2.1] e M1 82 [3.228] 17.5 [6.712] 87 [3.425] 18.5 [7.16] Model code examples and maximum shaft torque Flange/drive gear configuration Model code example 2F SNP3NN/44RN2FP1CCNNNN/NNNNN 21 [1858] 2D SNP3NN/33RN2DP1CC7NNNN/NNNNN 29 [2566] 2B SNP3NN/26LN2BP1C7C7NNNN/NNNNN 35 [397] For further details on ordering, see Model Code, pages 8 9. Maximum shaft torque N m [lb in] L February 211 Rev B

28 Dimensions SNP3NN 3FB, 3BB This drawing shows the standard porting for 3FB and 3BB. 5 [1.968] Ø 22 [.866 ] FB 59 [2.323] 9 [.354] (full thd 18 [.78] deep) Distance from front flange to shoulder Nut and washer supplied with pump Recommended tightening torque: Nm - 5 [.196 ] 24 [.945 ] Ø6.3 [2.374 ] X ±.5 [.875 ±.2] 17.5 [.689] Ø 25 [.984] M16x1.5-6g 28.5 [1.122] 1:8 B-B 4.79 [.189 ] [2.362] 28 [1.12] 8 [.315] B B M1 (full thd 17 [.669] deep) [.532 ] 3BB B max 14.5 [.571] Distance from front flange to cone reference diameter 22 [.866] ±.75 [±.3] C/c E/e (149.5 [ 5.885]) D/d ±.25 [±.1] 1 [ 3.937] ±.75 [1.75 ±.3] [ 1.949] Ø.75 [.3] X [5.768] max [4.5] 115 ±.25[4.5 ±.1] body width [ ] 148 [ 5.826] max 116 [4.566] max 65.5 [2.578] max [ 7.145] max mm [in] SNP3NN 3FB and 3BB dimensions Type (displacement) Dimension Inlet Outlet B 63. [2.48] [5.216] 64.5 [2.539] [5.334] 67. [2.637] 14.5 [5.531] 68.8 [2.78] 144. [5.669] 71. [2.795] [5.846] 72.5 [2.854] [5.964] 75. [2.952] [6.161] 78. [3.7] [6.397] C 2 [.787] [1.63] 36 [1.417] D 4 [1.575] 51 [2.7] 62 [2.441] E M1 c 2 [.787] [1.63] d 4 [1.575] 51 [2.1] e M1 82. [3.228] 17.5 [6.712] 87. [3.425] 18.5 [7.16] Model code examples and maximum shaft torque Flange/drive gear configuration Model code example 3FB SNP3NN/44LN3FBP1CCNNNN/NNNNN 3 [26] 3BB SNP3NN/9RN3BBP1CDCNNNN/NNNNN 5 [4425] For further details on ordering, see Model Code, pages 8 9. Maximum shaft torque N m [lb in] 28 L February 211 Rev B

29 Dimensions SNP3NN 6DD, 6 This drawing shows the standard porting for 6DD and 6. 6DD 6 51 [2.7] B max mm [in] Ø [ ] 7 [.5] 28 [1.12] 4 [1.574] Distance from front flange to shoulder Ø15 [4.133 ] X ±.5 [.874 ±.2] 23.5 [.925] 15 [.59] [.433] [.984] Ø 25 [.984] M16x1.5-6g 1:5 8 [.314] 22 [.866] 45 o ±.75 [±.3] C/c (145 [5.78]) 97 [3.818] 48 [1.889] 115 ±.25 [4.5 ±.1] body width 148 [ 5.826] max (18 [4.251]) (58.5 [2.33]) [ 6.5] max Spline: B28x25 DIN 5482 (Profile offset:.22 [.8]) Nut and washer supplied with pump Recommended tightening torque: Nm [ ] E/e (full thd 12 [.472] deep) [.512 ] D/d ±.25 [.1] Ø.75 [.3] X [ ] 12. [4.15] [4.862] max SNP3NN 6DD and 6 dimensions Type (displacement) Dimension Inlet Outlet B 63. [2.48] [5.216] 64.5 [2.539] [5.334] 67. [2.637] 14.5 [5.531] 68.8 [2.78] 144. [5.669] 71. [2.795] [5.846] 72.5 [2.854] [5.964] 75. [2.952] [6.161] 78. [3.7] [6.397] 82. [3.228] 17.5 [6.712] C [1.63] 36 [1.417] D E c 18 [.78] [1.63] d e 87. [3.425] 18.5 [7.16] Model code examples and maximum shaft torque Flange/drive gear configuration Model code example 6DD SNP3NN/44RN6DDP1BBBNNNN/NNNNN 45 [3982] 6 SNP3NN/26LN6P1BBBNNNN/NNNNN 3 [26] For further details on ordering, see Model Code, pages 8 9. Maximum shaft torque N m [lb in] L February 211 Rev B 29

30 Dimensions SNP3NN and SEP3NN 7S, 7G The drawing shows the SNP3NN standard porting for 7S and 7G. The same configurations are available for the SEP3NN. 7S B max 7G 41.2 [1.622] [6.948] max mm [in] 41.2 [1.622] ±.75 [±.3] [5.75] 7.9 [.311] 33.3 [1.311] 7.9 [.311] 33.3 [1.311] R 61 [2.42] max Ø [ ] 25. [.984] C/c E/e ±.25 [.1] -1.5 [.59] Splined: SE J498-13T-16/32DP Flat root side fit (circular tooth thickness.1 mm [.5] less than standard class 1 fit) 13.5 [.531] 9.5 [.374] F/f (full thd 2 [.787] deep) D/d ±.25 [.1] [.25-.1] Ø [ ] ±.5 [.874 ±.2] Ø [ ] X [.7-.58] Ø.75 [.3] X 115 ±.25 [4.5 ±.1] body width 157 [ 6.181] max [ ] The SEP3NN overall length is 12 mm [.472 in] less than the SNP3NN for the whole range of displacements (22.1 to 44.1 cm 3 /rev [1.35 to 2.69 in 3 /rev]). SNP3NN, SEP3NN 7S and 7G dimensions Type (displacement) Dimension Inlet Outlet B 63. [2.48] [5.216] 64.5 [2.539] [5.334] 67. [2.637] 14.5 [5.531] 68.8 [ [5.669] 71. [2.795] [5.846] 72.5 [2.854] [5.964] 75. [2.952] [6.161] 78. [3.7] [6.397] 82. [3.228] 17.5 [6.712] C 25.4 [1] 31.8 [1.251] 38.1 [1.5] D [1.31] 3.18 [1.188] [1.45] E [2.61] [2.311] [2.75] F 3/ 8 16UNC 2B 7/ 16 14UNC 2B ½ 13UNC 2B c 19.1 [.751] 25.4 [1.] 31.8 [1.251] d [.875] [1.31] 3.18 [1.188] e [1.875] [2.61] [2.311] f 3/ 8 16UNC 2B 3/ 8 16UNC 2B 7/ 16 14UNC 2B 87. [3.425] 18.5 [7.16] 3 L February 211 Rev B

31 Dimensions SNP3NN and SEP3NN 7S, 7G (cont.) Model code examples and maximum shaft torque Flange/drive gear configuration Model code example 7S SNP3NN/63LN7SP154NNNN/NNNNN [2389] 7G SNP3NN/26LN7GP132NNNN/NNNNN 23 [235] Maximum shaft torque N m [lb in] For further details on ordering, see Model Code, pages 8 9. L February 211 Rev B 31

32 OpenCircuitGear Our Products Turolla OpenCircuitGear luminum Gear Pumps luminum Gear Motors Cast Iron Gear Pumps Cast Iron Gear Motors Fan Drive Gear Motors luminum Fan Drive Gear Motors Cast Iron TurollaOCG, with more than 6 years of experience in designing and manufacturing gear pumps, gear motors and fan drive motors of superior quality, is the ideal partner ensuring robustness and reliability to your work functions. We are fast and responsive - the first to specify a customer product, the most experienced in providing technical knowledge and support for fan drive solutions. We offer a lean value chain to our partners and customers and the shortest lead time in the market. TurollaOCG is member of the Sauer-Danfoss Group. Local address: Turolla Via Villanova Villanova di Castenaso Bologna, Italy Phone: Fax: Turolla Kukučínova Považská Bystrica, Slovakia Phone: Fax: Turolla 28 East 13th Street mes, I 51 US Phone: Fax: L February 211 Rev B

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