Tuthill 1012 Quick guide

Installation and Service Instructions
Excellence at work. Excellence in life.
1012, 1014, 1015, & 1017 Size Pumps

Page 2 of 9
Table of Contents
General Description 3
The Pumping Principle 3
Location 3
Proper Installation 4
Filter Protection 4
Startup 5
Disassembly of Seal 5
Disassembly of Pump 6
Inspection 6
Reassembly of Pump 6
Pump Selection 7
1012 - 1022 Parts List 8
Field Checklist 8
Material Returns 9

Page 3 of 9
General Description
Both types can be supplied with automatic reversing (Style “R”), feature steam jackets (through which steam or other heating medium
may be forced to melt or reduce viscosity of materials to permit rotation of the pump at starting. Conversely, when desirable, cooling
water may be forced through these jackets). These pumps can also be supplied with an integral relief valve. Nitrile, Neoprene and Viton
seals are available with these units along with P.T.F.E. or Mellinex gaskets. When pumping temperatures in excess of 1000c are used,
special H.T. gaskets are also available.
The Pumping Principle
Tuthill internal-gear principle is based upon the use of a rotor, idler gear and crescent shaped partition that is cast integrally with the
cover. (See accompanying gure). Thus, only two moving parts comprise this ecient pumping element. Power is applied to the rotor
and transmitted to the idler gear with which it meshes. The space between the outside diameter of the idler and the inside diameter of
the rotor is sealed by the crescent. When the pump is started, there is an increase in volume as the teeth come out of mesh. This creates
a partial vacuum, drawing the liquid into the pump through the suction port. The liquid lls the space between the teeth of the idler and
rotor and is carried past the crescent partition to the pressure side of the pump. When the teeth mesh on the pressure side, the liquid
is forced from the spaces and out through the discharge port.
WARNING
Failure to follow these instructions could result in serious bodily injury or death. These pumps should not be used for handling plain
water, corrosive/abrasive liquids, or liquids not possessing adequate lubricity. Do not attempt to work on any Tuthill pump installation
before completing the steps below. Disconnect the drive so that it cannot be started while work is being performed. Review the Material
Safety Data Sheet (MSDS) applicable to the liquid being pumped to determine its characteristics and the precautions necessary to
ensure safe handling. Vent all pressure within the pump through the suction or discharge lines. All Tuthill pumps contain residual ISO
32 lube oil from the factory production test. Determine if this is compatible with the uid you are pumping. If the uid is incompativle
please consult factory directly.
Location
The pump should be located as close to the source of supply as conditions will permit, below the level of the liquid in the reservoir, if
possible. Pumps should be located in a dry and clean place, with space to work around them.
When necessary to locate pumps in pits, provisions should be made to safeguard against oods. Care must be taken to properly support
the suction and discharge piping so that no strain can be put on the pump from either its weight or expansion. Piping strains are very
often the cause of misalignment, hot bearing, worn couplings and vibrations.

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Proper Installation
A large percentage of unsatisfactory pump installations is caused by failure to observe the natural laws limiting the suction lifts on
volatile materials. At temperatures of approximately 70°F or lower, kerosene and light fuel oils may be pumped at nearly full volumetric
eciency when combined vertical lift and friction in the suction line do not cause a vacuum to exceed 10 inches of mercury at the
suction port of the pump. Ten inches vacuum on kerosene oil is equal to approximately fourteen feet of vertical lift without pipe friction.
This varies with the temperature and various oils, but if, in laying out the suction line, the maximum vacuum is kept at this gure or
lower, good results may be expected. If this vacuum is exceeded, it is almost certain to result in cavitation, loss of volume and a noisy
installation.
When pipelines are installed, an inverted “U” bend should be incorporated in the suction line close to the pump to trap liquid in the
pump for priming. The suction line must be kept free from air leaks and air pockets.
When handling liquids of high viscosity, such as asphalt, heavy gear lubricants, linseed oil, Bunker “C” fuel oil, molasses, etc., the speed
of the pumps and the running clearances are important. Consult Tuthill UK, whenever unusual conditions of speed, pressure, vacuum
or viscosity are encounted.
Before initial start of the pump, it is recommended that some of the liquid to be pumped be introduced into the pump ports to insure
wetting of the rotation elements. Check alignment and rotation of the driver to see that pump will rotate in the designated proper
direction of rotation.
Filter Protection
Piping or tubing should be cleaned out thoroughly to remove chips and pipe scale before connecting the piping to the pump. Neglect
of this precaution may result in damage to the pump when it is put in operation. The suction piping should be as short and direct as
possible. Grit, pipe chips, or other foreign substance that is allowed to pass through the, pump, will almost surely injure and possibly
ruin it. Always remember the following in the selection and position of a lter.
• A lter should be installed to protect the pump whenever conditions permit
• When uncertain of pressure drop through the lter, obtain this data from manufacturer, giving pump capacity and type of
liquid to be handled
• Install lter according to arrows or notation designating ow
• Have lter accessible for servicing
• Use duplex type where shutdown during servicing is not permitted
• Provide a vacuum gauge in the suction line for determining when the lter requires cleaning
• The greater the free opening, the less attention the lter will require
WARNING
All Tuthill pumps contain resigal ISO 32 lube oil form the factory production test. Determine if this is compatible with the uid you are
pumping. If the uid is incompatible please consult factory directly. If the pump is to operate at elevated temperatures, it should be
brought up to operating temperature gradually. Rapid or sudden introduction of liquid at an elevated temperature into the cold liquid
chamber of the pump could cause damage to the seal or other internal parts. Do not run the pump dry. This could cause severe damage
to the seal, bushings, and/or metal parts. Temperatures must not exceed 200°C without prior consent

Page 5 of 9
Startup
Prior to starting the pump double check the following.
• Pressure and vacuum gauges should be installed as close as possible to the pump
• Rotate pump shaft to ensure it turns freely without binding
• Recheck alignment and ensure all guards are in place
• Make sure piping is independently supported and no strain is being transmitted to the pump
• Make sure the safety relief valve is installed correctly
• Check pump rotation
• Open suction and discharge gate valves
• Check for any leaks once gate valves are open
CAUTION
The pump should not be run dry. If after approximately 60 seconds there is no discharge of liquid, stop the pump and investigate the
possible cause. Failure to comply with this could cause severe damage to internal seals, bushings and/or metal parts.
WARNING
Failure to follow these instructions could result in serious bodily injury or death. Do not attempt to work on any Tuthill pump installation
before completing the steps below. Disconnect the drive so that it cannot be started while work is being performed. Review the Material
Safety Data Sheet (MSDS) applicable to the liquid being pumped to determine its charaacteristics and the precautions necessary to
ensure safe handling. Vent all pressure within the pump through the suction or discharge lines. All Tuthill pumps contain residual ISO
32 lube oil from the factory production test. Determine if this is compatible with the uid you are pumping. If the uid is incompatible
please consult factory directly.
Disassembly of Seal
The seal assembly of the pump may be changed without the disassembly of the rest of the pump.
1. Deburr shaft especially around the keyway area.
2. Hold the pump in a vice, cover down and remove the grub screw from the lockable shaft bearing collar. Remove collar.
3. Unscrew the 3 o 6mm bolts to remove the bearing housing, (this may be tight due to the sealant used during assembly). This can
be done by holding the bearing housing and twisting the body.
4. Remove static seal plate from bearing housing, noting dowel pin in plate location face, and place to one side.
5. Undo the three grubscrews on the mechanical seal collar and gently pull o shaft, again put to one side. (Remove secondary collar
if there is one present.) Press out the seal housing bearing.
6. Inspect rotor, if badly scored in seal or bearing area, rotor should be replaced. Also check seal faces for the same scoring. Remove
0-rings and check for deformation, again replace if there is any doubt.
7. Clean all parts thoroughly and replaced static seal plate ensuring that the plate is positioned correctly over the dowel.
8. Ret collar to the shaft, using a 0.002” feeler gauge between the collar and ange (if it originally had one tted). Lubricate 0-ring
inside the mechanical seal with a light oil and guide down the shaft. If the pump had a collar then push the mechanical seal down
onto the collar and retighten the three grubscrews, if the pump did not have a collar then use a 0.002” feeler gauge between the
ange and the mechanical seal to create the correct end oat. And retighten the three grub screws.
9. Apply the new bearing housing gasket and ret the bearing housing.
10. Press in the lockable bearing. Take the lockable collar and place over bearing ensuring that it is fully located and while holding the
collar rotate the shaft clockwise. Take a 3/16th pin punch and gently tap the collar counterclockwise until the grubscrew lines up with
the indentation on the shaft and then retighten.

Page 6 of 9
Disassembly of Pump
1. Deburr shaft especially around the keyway area.
2. Hold the pump in a vice, cover down, and remove the grub screw from the lockable shaft bearing collar. Remove collar.
3. Unscrew the 3 o 6mm bolts to remove the bearing housing (this may be tight due to the sealant used during assembly). This can
be done by holding the bearing housing and twisting the body.
4. Remove static seal plate from bearing housing, noting dowel pin in plate location face, and place to one side.
5. Undo the three grubscrews on the mechanical seal collar and gently pull o shaft, again put to one side. (Remove secondary collar
if there is one present). Press out the seal housing bearing.
6. Mark the cover and body for orientation and hold in the vice with the shaft pointing downwards. Remove the 8 o 8mm cap head
screws and remove the cover assembly by pulling upwards, place to one side.
7. Making sure there is sucient clearance underneath the pump, (to prevent damage to the rotor vanes) press the rotor out through
the body.
8. The individual parts must now be inspected for damage. The keyway in the end of the rotor must be in good condition and there
must not be any deep scratches or grooves on the following surfaces.
• The ID surface of the housing and OD of the rotor
• The end face of the rotor
• The OD of the idler
• Both faces of the idler
• The inside surfaces of the cover including surfaces on the crescent
• Areas on the shaft of the rotor were the seal seats.
Inspection
Check cover, housing, rotor and idler for wear, chipped or broken teeth. Drop o in capacity is generally caused by the abrasive action
of foreign materials in the oil, resulting in end play of the rotor.
Check for side movement in the rotor assembly, as this indicates potential bearing failure.
Reassembly of Pump
1. Clean all parts thoroughly using great care to eliminate dirt.
2. Take the body and press the rotor assembly into it’s location ensuring that the bearing is square, check that the rotor turns freely in
the body.
3. Hold unit in a vice with the shaft pointing downwards.
4. Again using a new gasket and 0-ring t the cover.
5. Make sure the rotor turns freely.
6. Turn the unit over in the vice so that the rotor is pointing upwards again.
7. Ret collar to the shaft, using a 0.002” feeler gauge between the collar and ange (if it originally had one tted). Lubricate 0-ring
inside the mechanical seal with a light oil and guide down the shaft. If the pump had a collar then push the mechanical seal down
onto the collar and retighten the three grubscrews, if the pump did not have a collar then use a 0.002” feeler gauge between the
ange and the mechanical seal to create the correct end oat. And retighten the three grub screws.
8. Apply the new bearing gasket and ret the bearing housing.
9. Press in the lockable bearing. Take the lockable collar and place over bearing ensuring that it is fully located and while holding the
collar rotate the shaft clockwise. Take a 3/16th pin punch and gently tap the collar counterclockwise until the grubscrew lines up with
the indentation on the shaft and then retighten.

Page 7 of 9
Pump Selection
The above pumps are only suitable for liquids having self-lubricating properties. The table below shows the capacity and suggested
driving motor size for dierent speeds and pressures. These gures are based upon pumping a liquid of about 200 S.S.U. viscosity,
and with a 10-inch vacuum. While Tuthill pumps will develop as high as 27 inches of vacuum, it is sound engineering to reduce the
vacuum to a minimum. The speed of the pump must be reduced when handling liquids of high viscosity and the size on lines increased
to prevent cavitation, loss of capacity and high power requirements.
CAUTION
Remember that the pipeline friction increases at a rapid rate with increase in viscosity. For a given pump and motor, larger pipelines are
necessary to maintain the same pump pressure when changing from a thin liquid to a thick liquid. Viscous liquid pumping installations
are notoriously under powered, due to lack of knowledge in computing pipeline friction. Handling of viscous liquids is a special hydraulic
engineering problem, which the Engineering Department of Tuthill is well equipped to solve for you.
Consult Tuthill for selecting the proper pump, size of motor, and pipeline size for your job with the following information
• Capacity required
• Maximum and minimum liquid temperature when entering the pump
• The viscosity at the minimum temperature
• Total length of suction pipe and discharge pipe
• Suction lift and height to which the pump must force the liquid
Pump Speed 1424 RPM 960 RPM 720 RPM
Operating Pressure 10 PSI 50 PSI 100 PSI 10 PSI 50 PSI 100 PSI 10 PSI 50 PSI 100 PSI
GPM HP GPM HP GPM HP GPM HP GPM HP GPM HP GPM HP GPM HP GPM HP
1012 6 0.5 5.3 .75 4.6 1 4.3 .33 4 0.5 3.7 .75 3.3 .25 3 .33 2.7 .5
1015 12 1 11.2 1.5 10.5 2 8 0.5 7.7 1 7.3 1.5 6 .33 5.7 .75 5.3 1
1018 24.4 1.5 23.7 2 23 3 16 1 16.7 1.5 15.3 3 12 .75 11.7 1.5 11.3 2
1020 40.9 2 40.2 4 39.6 7.5 26.7 1.25 26 3 26.3 6 20 1 19.3 2 18.7 3
1022 55.4 3 54.7 5.5 54 10 37.3 2 36.7 4 36 7.5 28 1.5 26.7 3 25.3 4
1012 - 1022 Series Drawing
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Page 8 of 9
1012 - 1022 Parts List
Item Description Quantity Drawing
Number
Part
Number Material
1 Relief Valve 1 A112UK LXUK9219 Various
2 Cover 1 A1066UK 3M35-XUK9014 Cast Iron
3 O’Ring 1 BS046 Neoprene
4 Idler Gear 1 11002-A 3M5-1 Steel/Carbon
5 Body 1 1015-015 Cast Iron
6 Bearing 1 2RLS6/2RS
7 Mechanical seal 1 680-111-23AX12
8 Bearing 1 2RLS6/2RS
9 Circlip 1 NAM300-187
10 Rotor 1 A21445UK Steel
11 Seal Housing 1 1015-012 Cast Iron
12 Shims 2 0.006” Melonex
13 Idler Pin 1 5225-A 3M31 Steel
Field Checklist
1. No Oil is Delivered
• Suction lift too high for vapour pressures of liquid pumped
• While Tuthill Pumps will develop as high as 27 inches of vacuum, it is wise to reduce the vacuum to a minimum
• Bad leaks in suction line or port passages can be detected by submerging pressure line from discharge side of pump into a
pail of oil where the air will be seen in the form of bubbles
• Wrong direction of shaft rotation (In “R” models, check position of cover boss)
• Pump shaft not rotating (Check coupling or drive)
• Relief valve setting too low (Discharging uid through by-pass port)
2. Capacity is too Low
• Suction lift too high
• Air leaks in suction line
• Suction line too small (Can be detected by installing a vacuum gauge directly at the pump suction
• Pump speed too slow
• Filter too small or obstructed
• Suction pipe or port not immersed in the liquid deep enough
• Piping improperly installed, permitting air pocket to form in pump
• Increased clearance or wear in the pump will sometimes cause the pump to deliver an insucient supply of liquid
• A folded gasket or a slight amount of dirt not only will frequently exaggerate the original trouble but will also be the cause
of leakage
Note: The maximum vacuum at the pump suction should never exceed 15 inches of mercury. Not because of the inability of the pump
to handle a higher vacuum, but primarily because the vaporization that is liable to take place at a higher vacuum. Vaporization caused
by higher vacuums will generally result in capacity drop-o.

Tuthill Pump Group
12500 S. Pulaski Road, Alsip, IL 60803
www.tuthillpump.com Excellence at work. Excellence in life.
3. Pump Works Spasmodically
• Leaky suction lines
• Suction lift too high
• Air or vapour in liquid
• Coupling slipping on pump shaft.
4. Pump Wastes Power
• Pressure too high
• Liquid more viscous than desired
• Suction or discharge lines obstructed
• Mechanical defects (End thrust on pump shaft)
• Drive shaft and pump shaft misaligned
• The pump may be binding due to insucient end clearance
• Pump shaft bent
• Misalignment within pump due to bad piping or poor installation, causing strains or distortion
Note: Tuthill pumps are not designed to take end thrust toward the pump cover and care must be taken to prevent thrust in this
direction.
5. Pump is Noisy
• Machine or part of it is acting as a sounding board
• Misalignment or bad design of coupling
• Coupling set too close to pump
• Vibration of pump because of bent shaft or worn parts
• Air leaks on suction side of pump
• Suction lift too high, causing vaporization.
6. Pump Leaks
• Cover bolts need tightening, or cover gasket is defective
• Seal is defective or worn
Material Returns
If it becomes necessary to return a pump to the factory, a Return Goods Authorization (RGA) must be obtained from either your local
Authorized Distributor or our plant. No RGA can be issued until a completed Material Safety Data Sheet (MSDS) has been forwarded to
our plant and return of the pump approved.
• Tuthill pumps are precision built and must be handled with care
• Pumps must be drained of all uid and the ports plugged to prevent foreign material from getting into the pump
• Pumps must be packaged securely to prevent damage while in transit