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Allweiler AE1L Series Manual

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1
Operating and Maintenance Instructions VM No.: 760.0002 GB
with Dismounting and Edition: 02.04
Mounting Instructions Ident No.: 150 500
Eccentric Screw Pumps
Series AE1L, AE.E, AE.N, AE.H, AE.V,
AED1E, AED2N
Design ID, ZD
Order No.: Ident No. of Pump:
Machine No.: Pump Type:
Operating data, dimensions and other additional information can be found in the order-specific part of the documentation.
Contents
1. General
2. Safety
3. Transport and Intermediate
Storage
4. Description
5. Installation/Mounting
6. Start-up/Shutdown
7. Maintenance/Repair
8. Operating Faults, Causes
and Remedial Action
Important note:
This operating manual is to be supplemented
by the order-related information.
Retain
for future
use!
These Operating and Maintenance In-
structions contain information from the
pump manufacturer. They may need to
be supplemented by instructions of the
operator company for its personnel.
These instructions do not take account
of specific information relating to opera-
tion and maintenance of the process
plant into which the pump is integrated.
Such information can only be given by
the persons responsible for construction
and planning of the plant (plant manu-
facturer).
Such specific instructions relating to
operation and maintenance of the
process plant into which the pump is
integrated have priority over the in-
structions of the pump manufacturer.
The plant manufacturer must on princi
-
ple observe the limits of use!
Refer to the operating instructions of th
e
plant manufacturer!
2
Baureihen AE1L, AE.E, AE.N, AE.H, AE.V, AED1E, AED2N
Bauform ID, ZD
Table of Contents
1. General
1.1 Application and range of utilization
1.2 Performance data
1.3 Abbreviation
1.4 Warranty
1.5 Testing
2 . Safety
2.1 Marking of hints in the operating instructions
2.2 Personnel qualification and personnel training
2.3 Dangers in case of non-compliance with the safety hints
2.4 Responsible working
2.5 Safety hints for the user/operator
2.6 Safety hints for maintenance, inspection and mounting
operations
2.7 Independent reconstruction and spare parts production
2.8 Inadmissible modes of operation
2.9 Operation in potentially explosive environments
3. Transportation and intermediate storage
3.1 Packing
3.2 Transportation
3.3 Preservation and storage of eccentric screw pumps
4. Description
4.1 Structural design
4.1.1 Bearing ans lubrication
4.1.2 Shaft seal
4.1.3 Dimensions/branch position/flanges
4.2 Sound pressure level
4.3 Mode of operation
4.4 Aggregate construction
4.4.1 Drive
4.4.2
Shaft coupling and protection against accidental
contact
4.4.3 Base plate
5. Installation/Mounting
5.1 Installation
5.2 Foundation
5.2.1 Arrangement of a steel foundation plate
5.2.2 Arrangement of concrete foundations
5.2.3
Fastening of the pump aggregate on the concrete
foundations
5.2.4
Arrangement of concrete foundations for poured
base plates
5.2.5 Pouring of base plate
5.3 Base plate
5.4 Coupling
5.5 Assembling of pump and drive
5.6 Drive by V-belt drive
5.7 Space required for maintenance and servicing
5.8 Installing of pipelines
5.8.1 Nominal widths
5.8.2 Supports and flange connections
5.8.3 Cleaning of pipelines prior to attachment
5.9 Installing of auxiliary pipelines for additional facilities
5.10 Safety and control facilities
5.10.1 Manometer and vacuumeter
5.10.2 Safety installation in the pressure pipeline
5.11 Electrical connections
6. Start-up/Shutdown
6.1 Preparations for start-up
6.1.1 Filling the pump with liquid
6.1.2
Turning on the additional facilities for shaft seals (if
provided)
6.1.3
Quality and properties of the flushing/sealing and
quenching liquid
6.1.4
Turning on the additional facilities for heating or
cooling the stuffing box casing and/or the suction
casing (double-jacket casing)
6.1.5 Breaking away of the pump
6.1.6 Control of the sence of rotation
6.2 Start-up
6.2.1 Start-up
6.2.2 Drive
6.2.3 Checking the delivery values
6.2.4 Protection against running dry
6.3 Shutdown
6.3.1 Shutoff
6.3.2 Measures in case of longer periods of standstill
7. Maintenance/Repair
7.1 Maintenance
7.1.1 General monitoring
7.1.2 Maintenance of components
7.1.2.1 Joints of the joint shaft
7.1.2.2
Bearing of the drive shaft and lubrication of the bear-
ings
7.1.2.3 Shaft sealing
7.1.2.4 V-belt drive
7.1.2.5 Drive engines and (variable speed gear) drive
7.1.2.6
Packing ring dimensions (for Chapter 7.1.2.3), lubri-
cant quantities for joints (for Chapter 7.1.2.1), bear-
ings (for Chapter 7.1.2.2) and flushing liquid flows
(for Chapter 6.1.2)
7.2 Repair (dismounting and mounting instructions)
7.2.1 Dismounting of the eccentric screw pump
7.2.1.1 Dismounting the stator
7.2.1.2 Dismounting the rotor and the rotor-side joint
7.2.1.3 Dismounting the joint shaft and the drive-side joint
7.2.1.4 Dismounting the shaft seal and the drive shaft
7.2.1.5
Dismounting the angular contact and groove ball
bearings
7.2.2 Mounting of the eccentric screw pump
7.2.2.1
Installing the angular contact and groove ball bear-
ings
7.2.2.2 Installing the shaft seal with dismounted drive shaft
7.2.2.3 Installing the drive shaft with shaft seal
7.2.2.4 Installing the rotor and rotor-side joint
7.2.2.5 Installing the joint shaft and the drive-side joint
7.2.2.6 Installing the stator
7.3 Replacement parts/spare parts
7.4
List of individual parts and recommended replacement
parts/spare parts
7.5
Sectional drawing for series AE1L, AE1E, AE2E, AE1N, AE2N,
AE4N, AED1E, AED2N; Design ID
7.6
Sectional drawing for series AE1+1H, AE2+2H, AE2+2V,
AE4+4V; Design ID
7.7 Sectional drawing for series AE2H, AE4H; Design ID
7.8 Sectional drawing for series AE1N, AE2N; Design ZD
7.9 Sectional drawing for series AE1+1H, AE2+2H; Design ZD
7.10 Sectional drawing for series AE2H, AE4H; Design ZD
8. Operating faults, causes and remedial action
3
Series AE1L, AE.E, AE.N, AE.H, AE.V, AED1E, AED2N
Design ID, ZD
1. General
1.1 Application and range of utilization
The eccentric screw pumps are self-priming, rotary
positive-displacement pumps for handling and dosing
low to high-viscosity, neutral or aggressive, pure or
abrasive, gaseous liquids or liquids which tend to
froth, even with fibre and solids contents.
The range of utilization is to be
taken from the order data sheet.
1.2 Performance data
The exact performance data applying to the pump
are to be taken from the order data sheet and are
engraved on the name plate.
1.3 Abbreviation
The abbreviation of the eccentric screw pumps is set
up according to the following scheme:
Example:
This abbreviation is embossed on the type plate.
1.4 Warranty
Our liability for shortcomings in the supply is laid down
in our delivery conditions. No liability will be under-
taken for any damages caused by non-compliance
with the operating instructions and service conditions.
If at any later date the operating conditions happen to
change (e.g. different liquid pumped, speed, viscosity,
temperature or pressure conditions), it must be
checked by us from case to case and confirmed, if
necessary, whether the pump is suited for these pur-
poses. In case no special agreements were made,
pumps supplied by us may, during the warranty pe-
riod, be opened or varied only by us or our authorized
contractual service stations; otherwise, our liability for
any defects will cease.
1.5 Testing
Prior to leaving our factory, all pumps are subjected to
a leakage and performance test. Only properly oper-
ating pumps leave the factory achieving the perform-
ances assured by us. Thus, compliance with the fol-
lowing operating instructions ensures proper opera-
tion.
2. Safety
These operating instructions contain basic hints to be
observed in case of installation, operation and main-
tenance. Therefore, prior to mounting and commis-
sioning, these operating instructions must by all
means be read by the fitter as well as the pertinent
expert personnel/customer and must always be avail-
able at the place of installation of the machine/ plant.
Not only are the general safety hints listed under this
main item „Safety“ to be observed, but also the spe-
cial safety hints such as for private use added to the
other main items.
2.1 Marking of hints in the operating instructions
The safety hints contained in these operating instruc-
tions which, in case of non-compliance, may cause
danger to personnel, are particularly marked with the
general danger symbol
in case of warning against electric voltage with
For safety hints, non-compliance with which may
cause dangers to the machine and its functions, the
word
is inserted.
Hints directly attached to the machine such as
! directional marker
! signs for fluid connections
must by all means be observed and maintained in
completely legible condition.
2.2 Personnel qualification and personnel training
The personnel for operation, maintenance, inspection
and mounting must have the corresponding qualifica-
tion for these operations. Range of liability, compe-
tence and the supervision of the personnel must be
exactly controlled by the customer. If the personnel do
not have the required knowledge, same must be
trained and instructed. If required, this may be ef-
fected by the manufacturer/ supplier on behalf of the
machine customer. In addition, it must be ensured by
the customer that the contents of the operating in-
structions are fully understood by the personnel.
2.3 Dangers in case of non-compliance with the safe-
ty hints
Non-compliance with the safety hints may result in
danger not only to persons, but also to environment
and machine. Non-compliance with the safety hints
may lead to the loss of any claims for damages. In
detail, non-compliance may, for example, entail the
following dangers:
4
Series AE1L, AE.E, AE.N, AE.H, AE.V, AED1E, AED2N
Design ID, ZD
! failure of important functions of the machine/plant
! failure of specified methods for maintenance and
servicing
! danger to persons by electrical, mechanical and
chemical influences
! danger to the environment by leakage of danger-
ous substances
2.4 Responsible working
The safety hints mentioned in these operating instruc-
tions, the current national rules for the prevention of
accidents as well as any internal working, operating
and safety regulations of the owner must be ob-
served.
2.5 Safety hints for the user/operator
! If hot or cold machine parts lead to dangers, these
parts must be protected against accidental contact
at the site.
! Protection against accidental contact for moving
parts must not be removed when the machine is
in operation.
! When operating pump aggregates in a dust-laden
environment (e.g. milling, chipboard manufacture,
bakeries), the surface of the pumps and motors
must be cleaned at regular intervals, depending
on local conditions, in order to maintain the cool-
ing effect and eliminate the possibility of sponta-
neous combustion. Please also see explosion pro-
tection regulations (BGR 104).
! Leakages (e.g. of the shaft seal) of dangerous
materials to be handled (e.g. explosive, toxic, hot)
must be discharged so as not to result in danger
to persons and the environment. Legal stipula-
tions are to be observed.
! Dangers by electrical energy are to be excluded
(for details with regard hereto, please refer e.g. to
the regulations of the VDE and the local energy
supply associations).
2.6 Safety hints for maintenance, inspection and mo-
unting operations
The customer shall see to it that all maintenance, in-
spection and mounting operations are performed by
authorized and qualified expert personnel who have
sufficiently informed themselves by thoroughly study-
ing the operating instructions.
Basically, operations at the machine must be per-
formed during standstill only. The mode of operation
for stopping the machine described in the operating
instructions must by all means be observed.
Pumps or aggregates handling noxious liquids must
be decontaminated.
Immediately upon completion of the operations, all
safety and protective devices must be mounted and
made operational again.
Prior to restarting, the items listed in Chapter “Prepa-
ration for start-up” are to be observed.
2.7 Independent reconstruction and spare parts pro-
duction
Reconstruction of or changes to the machine are only
admissible after consultation with the manufacturer.
Original spare parts and accessories authorized by
the manufacturer serve safety purposes. The use of
other parts may cancel the liability for the conse-
quences resulting therefrom.
2.8 Inadmissible modes of operation
The operating safety of the machine supplied is only
ensured with due application according to Chapter 1
“General” of the operating instructions. The limit val-
ues given in the data sheet must by no means be ex-
ceeded.
2.9 Operation in potentially explosive environments
Observe the instructions of the ATEX additional oper-
ating manual when operating the pump respectively
aggregate in potentially explosive environments.
3. Transport and intermediate storage
3.1 Packing
The symbols applied to the packing must be ob-
served.
During transportation and storage, suction and outlet
side and auxiliary connections of the pump must be
closed with plugs. During installation of the pump ag-
gregate, the plugs must be removed.
3.2 Transportation
The pump or pump aggregate is to be safely trans-
ported to the place of installation, if required by
means of lifting gear.
The regulation for lifting loads in accordance with
VBG 9a must be observed. Crane and sling
equipment must be adequately dimensioned.
Sling equipment must not be secured to the lifting
eyes of the motor, except as additional protection
against overturning in the event of nose-
heaviness.
When transporting the pump by crane, place the
stopper ropes safely around the suction casing. With
complete pump aggregates, an additional rope must
be slung around the drive engine.
The stopper ropes have to be slung around the pump
respectively pump aggregate so that these are ex-
actly balanced when lifted.
Transportation to and at the installation site
Make sure, that the unit is transported safely and in a
stable position. Overturning due to nose-heaviness
must be prevented.
Transport damages
Check the pump for damage on
receipt. Any damage detected must
be notified immediately.
3.3 Preservation and storage of eccentric screw
pumps
Please refer to our document VM 2102/ …
5
Series AE1L, AE.E, AE.N, AE.H, AE.V, AED1E, AED2N
Design ID, ZD
4. Description
4.1 Structural design
Self-priming, one or two-stage eccentric screw pump.
The conveyor elements are rotor and stator. The input
torque is transmitted via the drive shaft and the joint
shaft to the rotor.
Pressure casing, stator and suction casing are held
together by external casing connection screws (clamp
bolts).
The stuffing box or mechanical seal housing is lo-
cated between the suction casing and the bearing
bracket.
4.1.1 Bearing and lubrication
Joint shaft with liquid-proof clad bolt joints. Greasing
with joint oil.
Bearing of the drive shaft in the bearing bracket
through greased angular contact and groove ball
bearings. Bearings protected against water jets.
4.1.2 Shaft seal
Through uncooled or cooled stuffing box or cooled or
uncooled, maintenance-free, non-released, singular
or double-acting mechanical seal.
4.1.3 Dimensions/branch position/flanges
The dimensions of the pump respectively the pump
aggregate, the branch position and flange dimensions
are to be taken from the tables of dimensions.
4.2 Sound pressure level
The sound pressure level of the pump is below 70 dB
(A).
4.3 Mode of operation
Self-priming, rotating positive-displacement pump.
Conveyor elements are the rotating helical rotor and
the static stator. Both touch in transection with series
AE.E, AE.N, AE.H, AE.V in two points each and with
series AE1L, AED1E, AED2N in three points each,
which form two sealing lines seen across the length of
the conveyor elements with series AE.E, AE.N, AE.H,
AE.V and three sealing lines with series AE1L,
AED1E, AED2N. The content of the sealed chambers
that form with the rotation of the rotor is shifted axially
and totally continuously from the suction to the outlet
side of the pump. No turbulence occurs despite the
rotation of the rotor. The unvarying chamber volume
rules out crushing forces and thus guarantees very
gentle, low-pulsation conveyance.
4.4 Aggregate construction
4.4.1 Drive
By means of non-explosion-protected or explosion-
protected electric motors, geared motors or variable
speed gear motors. Other drive variants (e.g. via V-
belts) are possible.
4.4.2 Shaft coupling and protection against accidental
contact
Shaft coupling according to DIN 740.
A protection against accidental contact according to
DIN EN 809 is attached as soon as the scope of sup-
ply comprises pump, base plate, shaft coupling and
drive.
According to the rules for the prevention of acci-
dents, the pump must be started only with a pro-
tection against accidental contact according to
DIN EN 809.
If a protection against accidental contact is not sup-
plied, same is to be installed by the operator.
4.4.3 Base plate
The pumps of horizontal installation are, as a rule,
mounted with the drive on a common base plate.
Base plates are provided of the steel type of construc-
tion.
5. Installation/Mounting
5.1 Installation
The pumps can be installed horizontally or vertically
with bearing upwards.
5.2 Foundation
The foundation design depends on the size of the
pump and/or the pump aggregate and the local instal-
lation conditions.
For exact data on the pump and aggregate dimen-
sions, please refer to our tables of dimensions.
The foundation may be designed as concrete founda-
tion or load-carrying foundation frame, for example of
the steel type.
All foundation designs are subject to the following:
The foundation must be designed so that it can take
the weight of the pump aggregate on the entire sur-
face.
5.2.1 Arrangement of a steel foundation plate
A steel foundation plate must be designed in such a
way that the base plate makes full contact and can be
secured with bolts or by welding.
If only some of the areas of the
base plate are supported, the plate
sags in the center or the pump aggregate can be
twisted. This influences the alignment of the pump
aggregate can cause high noise emission and dam-
age.
5.2.2 Arrangement of concrete foundations
Concrete foundations must be horizontal, straight and
clean and must fully absorb the load exerted on the
foundations. Concrete foundations must be designed
in such a way that the base plate makes full contact
and can be secured with suitable bolts (see our ag-
gregate drawing).
If only some of the areas of the
base plate are supported, the plate
sags in the center or the pump aggregate can be
twisted. This influences the alignment of the pump
aggregate and can cause high noise emission and
damage.
5.2.3 Fastening of the pump aggregate on the concrete
foundations
After aligning the pump aggregate on the concrete
foundations the securing bolts are diagonally and
evenly tightened.
5.2.4 Arrangement of concrete foundations for poured
base plates
When shuttering the concrete foundations it must be
observed that a gap for aligning the pump aggregate
and applying the mortar compound remains between
the top of the finished foundation block and the bot-
tom of the base plate.
6
Series AE1L, AE.E, AE.N, AE.H, AE.V, AED1E, AED2N
Design ID, ZD
The set concrete foundations must be straight, even
and clean. Any traces of oil must be removed from
the foundations. The recessed anchor holes for the
foundation bolts must be cleaned and removed and
cleaned out with air. Prior to the installation of the
pump aggregate the surface of the concrete founda-
tions must be roughened and cleaned to ensure a
good bonding between the foundation block and the
mortar compound.
5.2.5 Pouring of base plate
After alignment on the concrete foundations , a low-
shrinkage mortar compound must be poured over the
entire length of the base plate, covering also the an-
chor holes with the connected foundation bolts.
Once the mortar compound has set on the base plate
and in the anchor holes, the foundation bolts must be
diagonally and evenly tightened.
Note: When pouring or adding the mortar compound
it must be observed that the base plate makes full
contact. Tap the plate to ensure that no cavities have
formed underneath.
5.3 Base plate
The base plate must be fixed on the foundation, ten-
sion-free.
5.4 Coupling
A pump aggregate supplied complete was carefully
mounted at the factory. As the pump and the drive are
fixed on the base plate, re-alignment of the coupling is
not required.
5.5 Assembling of pump and drive
If the aggregate is first completed on site, you need to
assemble the clutch as follows:
1. Thinly coat the pump and drive shafts with molyb-
denum sulfite (e.g. Molykote) and insert the
feather keys.
2. Wind up the pump and the motor-side clutch half
with the aid of a windup device so far until the
shaft end is aligned with the clutch hub. If no
windup device is available, heating the clutch
halves to approx. 100°C (without rubber buffers)
eases sliding on.
3. Fixate the clutch halves axially with a grub screw
(DIN 916).
4. When assembling the pump and the motor, the
drive motor respectively variable speed gear,
make sure that the clutch halves are exactly
aligned and that the distance between the cou-
pling halves is observed (see our aggregate draw-
ings and the details by the clutch manufacturers).
5. Install a contact protection in acc. with DIN EN
809.
5.6 Drive by V-belt drive
In case of a V-belt reduction from drive to pump,
make sure that two V-belt pulleys are aligned in paral-
lel.
The V-belt pulleys must be pushed onto the shaft
ends as far as possible. It must be possible to regu-
late the tension of the V-belts by means of a motor
rocker or by means of tensioning rails. They must be
slightly retightened after a short running-in period.
Excessive tensioning will destroy
the rolling bearings of the pump.
Our separate instructions “V-belt drive” (VM 706.0001
GB, Ident No. 133586) must be complied with.
5.7 Space required for maintenance and servicing
The pump must be accessible from
all sides in order to be able to per-
form the required sight inspections.
There must be enough room for maintenance and
service work, especially for the exchange of the con-
veyor elements. The stator and rotor dismounting di-
mensions are listed in the pump respectively pump
aggregate dimension sheet. Also make sure that all
pipelines can be attached/detached without obsta-
cles.
5.8 Installing of pipelines
5.8.1 Nominal widths
The nominal widths of the suction and pressure pipes
should be designed according to the nominal widths
of the pipe connections. Gross deviations, especially
on the suction side, require consultation with the fac-
tory.
5.8.2 Supports and flange connections
The pipelines must be connected tension-free to the
pump via the flange connectors. They have to be
supported near the pipe and should be easy to screw
on in order to avoid strains. After loosening the
screws, the flanges may neither be slanted nor
springy and also not rest on each other under pres-
sure. Possible thermal stress on the pipelines has to
be kept away from the pump by means of suitable
measures, e.g. the installation of compensators.
5.8.3 Cleaning of pipelines prior to attachment
The pipelines, sliders and valves on the suction side
must be rinsed respectively cleaned under all circum-
stances before installing the pump.
Leftover assembly parts like screws, nuts, welding
beads, pieces of steel, etc. destroy the inside parts of
the pump. Any warranty claim is void when damages
are caused by such leftover materials. Flange seals
may not protrude to the inside. Blind flanges, stoppers
protective foils and/or lacquers on flanges and sealing
strips have to be completely removed.
5.9 Installing of auxiliary pipelines for additional fa-
cilities
All auxiliary pipelines for supplying the shaft seal and
the possible double jacket casing for heating and
cooling the pump have to be connected tension-free
and sealing.
The pipes for the quenching liquid with single-acting
mechanical seals with quench (design: G0Q and
G1Q) and the sealing liquid with double-acting me-
chanical seal (design: G0D/G1D) should be installed
with a large flowtrough profile. The quenching respec-
tively sealing liquid discharge takes place at the high-
est connection of the mechanical seal housing.
The flow direction of the flushing, sealing and quench-
ing liquid is indicated with arrows in the section draw-
ings.
In order to ensure self-deairing, the pipes must be in-
stalled continuously rising, short and favorable for the
flow.
The formation of air pockets and gas bubbles has to
be prevented, install deairing connections if required.
The heating/cooling liquid discharge must be con-
nected to the highest connection of the possible dou-
ble-jacket casing.
7
Series AE1L, AE.E, AE.N, AE.H, AE.V, AED1E, AED2N
Design ID, ZD
5.10 Safety and control facilities
5.10.1 Manometer and vacuumeter
A manometer and vacuumeter have to be connected
to the pressure and suction pipe.
5.10.2 Safety installation in the pressure pipeline
As soon as a stop valve is arranged in the pressure
pipeline or if it is possible that the pressure pipeline
will be clogged, a safety element must be provided,
e.g.: by-pass line with installed excess pressure
valve, bursting diaphragm, protective motor switch
etc.
Eccentric screw pumps are positive-displace-
ment pumps and can theoretically generate an
infinitely high pressure.
In case of a closed pressure pipe, e.g. because of
clogging or accidental closing of the valve, the
pressure generated by the pump may reach a
multiple of the admissible plant pressure. This
may cause pipes to burst, which must be espe-
cially prevented when handling dangerous con-
veyor substances. Therefore, the corresponding
safety equipment (e.g. pressure switches) also
has be installed in the plant.
5.11 Electrical connections
Only an expert may attach the power cables of the
coupled drive engine in accordance with the circuit
diagram of the engine manufacturer. The valid guide-
lines of the Electrician's Association and the public
power companies have to be observed.
Danger by electrical energy must be excluded.
6. Start-up/Shutdown
6.1 Preparations for start-up
6.1.1 Filling the pump with liquid
The pump may not run dry! For
initial start-up and after longer peri-
ods of standstill, the pump must be filled with liquid.
Even a few rotations without liquid may damage the
stator. For that reason, the suction casing must be
filled with water or conveyor liquid prior to start-up for
lubricating the stator and rotor. After long periods of
standstill, meaning when it must be assumed that the
residual liquid in the pump has evaporated or after re-
pairs, you have to repeat the filling process.
After filling, the pump works in self-priming mode.
Deairing is not necessary, as the pump can convey a
liquid-gas mixture.
6.1.2 Turning on the additional facilities for shaft seals
(if provided)
If the pumps are charged with a flushing/sealing or
quenching liquid, the provided shut-off slides must be
opened before putting the pump into operation for the
first time and set to the following pressure values:
! Supply of the stuffing box with flushing or
sealing liquid (Design P02, P12, P03, P13, P04
and P14).
Note: Stuffing box with flushing or sealing cham-
ber ring require a flushing respectively sealing liq-
uid for maintaining the function.
The required flushing respectively sealing liquid
pressure for pumps with stuffing box is
P02/P12 = 0.1 to 0.5 bar
(above inner pressure of the suction casing)
P03/P13 = 0.5 bar
(above inner pressure of the suction casing)
P04/P14 = 0 to 0.5 bar
(Flushing and sealing liquid see Chapter 6.1.3.).
! Supply of single-acting, non-relieving me-
chanical seal with throttle ring (Design G0S/
G1S and G0T/G1T)
Note: These mechanical seals require a flushing
liquid in order to maintain their function, which car-
ries off the emerging friction heat and limits the
penetration of the conveyor liquid into the sealing
chamber.
The required flushing liquid pressure is 0.1 to 0.5
bar above the inner pressure of the suction cas-
ing. The required flushing liquid flow for carrying
off the dissipation of the mechanical seal is listed
in the table in Chapter 7.1.2.6 (flushing liquid see
Chapter 6.1.3).
! Supply of double-acting, non-relieving me-
chanical seal (Design G0D/G1D)
Note: These mechanical seals require a sealing
liquid in order to maintain their function, which car-
ries off the emerging friction heat and limits the
penetration of the conveyor liquid into the sealing
gap.
The circulation of the sealing
liquid must be secured prior to
each start-up.
The sealing liquid pressure must be approx. 1.5 to
2 bar above the pressure on the inside of the suc-
tion casing. The flowthrough quantity must be
regulated in such a way that the exit temperature
does not exceed approx. 60°C and is at least 30 K
below the boiling temperature at operating pres-
sure. The temperature difference between input
and output may amount to at most 15 K. (Sealing
liquid see Chapter 6.1.3).
! Supply of the single-acting mechanical seal
with quench (Design G0Q and G1Q)
The space between the mechanical seal counter-
ring and the shaft seal ring must be charged with
quenching liquid. The max. admissible pressure
difference between the quenching liquid pressure
and the pressure in the suction casing is p = 0,5
bar. The max. quenching liquid pressure is 3 bar.
(Quenching liquid see Chapter 6.1.3).
6.1.3 Quality and properties of flushing/sealing and
quenching liquid
Any liquid may be used as
sealing/flushing or quenching liquid
under consideration of the corrosion resistance of all
touching parts and the compatibility with the medium
to be sealed. The liquid must be free from solid sub-
stances, may not be prone to deposits, should have a
high boiling point as well as a good heat conductivity
and low viscosity. Clean and soft water fulfils these
requirements to a high degree.
8
Series AE1L, AE.E, AE.N, AE.H, AE.V, AED1E, AED2N
Design ID, ZD
6.1.4 Turning on the additional facility for heating or
cooling the stuffing box casing and/or the suction
casing (double-jacket casing)
If the pumps are equipped with these additional fea-
tures, all shut-off devices for heating or cooling sys-
tems must be opened. The following pressure and
temperature limits must be observed.
! Supply of the cooled or heated stuffing box
and/or suction casing (double-jacket casing)
with suitable liquid media
Only liquid media may be used as heating or
cooling liquid under consideration of the corrosion
resistance of all touching parts.
The maximum heating or cooling liquid pressure
is 6 bar. The maximum heating temperature may
not exceed 150°C and the cooling temperature
may not be below -40°C.
Note: The design temperature is listed in the or-
der data sheet.
6.1.5 Breaking away of the pump
When initially starting the pump or after longer periods
of standstill, you have to make sure that the drive en-
gine turns the pump effortlessly. Should this not be
easily possible due to the high adhesion between the
rotor and the stator in new state, use suitable tools on
the feather key section of the drive shaft to free the
pump.
The drive shaft may not be
damaged here!
6.1.6 Control of the sence of rotation
The normal rotation direction of the pump seen from
the drive against the drive shaft is to the left. Here the
suction connection is located on the side of the shaft
seal so that the shaft seal is relieved. In special
cases, e.g. when sucking from a vacuum or convey-
ing media that do not tolerate gas cavities, the pump
rotates to the right. This switches the suction and the
outlet side around.
The rotation direction of the pump
must correspond to the rotation
direction arrow "n" on the pump's type plate. A wrong
rotation direction may cause damages to the pump. In
order to control the rotation direction, briefly press the
on/off switch of the engine.
6.2 Start-up
6.2.1 Start-up
Prior to starting the pump, all shut-off devices on the
suction and outlet side have to be opened.
6.2.2 Drive
Turn the motor on.
Observe the product-specific peculi-
arities of the drive. See operating
instructions of the drive manufacturer.
6.2.3 Checking the delivery values
Once the drive has reached its operating speed,
check the intake pressure and the pump end pres-
sure via the vacuometer and the manometer.
The motor may not be overloaded. The power intake
can be monitored with an ammeter. Check the tem-
perature and the viscosity of the conveyor liquid in this
context. The resulting values must be compared with
the order data sheet respectively acceptance proto-
col.
6.2.4 Protection against running dry
When no more conveyor media is sucked in by the
pump, the thermal energy emerging in the conveyor
elements of the eccentric screw pump through dry
friction and milling work is no longer carried off in a
sufficient quantity, which thermally destroys the stator
elastomer after a short time already. There are differ-
ent protectors against running dry for protecting the
conveyor elements that are adapted to the respective
operating conditions (consultation with the factory).
6.3 Shutdown
6.3.1 Shutoff
Turn the motor off.
6.3.2 Measures in case of longer periods of standstill
If longer operational breaks are intended and if there
is danger of frost, the pump must be emptied. To do
so, unscrew the screw plug (502) from the suction
casing (505) and afterwards conserve the pump (see
Chapter 3.3).
7. Maintenance/Repair
7.1 Maintenance
! For service and maintenance work, observe the
details in Chapter 2 “Safety”.
! Regular monitoring and maintenance work on the
pump and the drive extends the service life.
7.1.1 General monitoring
1. The pump may not run dry.
2. The drive engine may not be overloaded.
3. Check the suction and pressure pipes for tight-
ness.
4. An installed stuffing boxmust drip slightly during
operation. An installed mechanical seal may not
have any strong leaks.
5. Monitor pressure and temperature monitoring de-
vices and compare them with the order data sheet
respectively acceptance protocol.
6. Additional installations like flushing, sealing and
quenching of the shaft seal must be monitored if
provided.
7. Additional equipment for heating or cooling the
stuffing box casing and/or suction casing must be
monitored, if provided.
7.1.2 Maintenance of components
7.1.2.1 Joints of the joint shaft
The joints of the joint shaft are lubricated with
ALLWEILER special joint oil type B or oil ET1510 ISO
460 by Tribol Lubricants GmbH, Mönchengladbach, if
the pumps are deployed in the food industry, with
ALLWEILER special joint oil type BL or oil 1810/460
by Tribol Lubricants GmbH, Mönchengladbach.
Other lubricants were not tested by
us and can therefore not be recom-
mended!
The joints are lubricated for life. We do however rec-
ommend checking the joint collar for tightness when
opening the pump for other reasons and exchanging
the joint oil after 8,000 operating hours. The table in
Chapter 7.1.2.6 shows the allocation of the pump size
to the oil quantity in cubic centimeters. For changing
9
Series AE1L, AE.E, AE.N, AE.H, AE.V, AED1E, AED2N
Design ID, ZD
the joint oil, refer to the disassembly and assembly in-
structions.
7.1.2.2 Bearing of the drive shaft and lubrication of the
bearings
Bearing of the drive shaft in the bearing bracket
through re-greasable angular contact and groove ball
bearings.
Note: The groove ball bearing is greased for life with
vertical pump installation.
Roller bearing lubricants
We recommend the following roller bearing lubricants
or others of a proven similar quality for lubricating the
ball bearings. The sequence of manufacturers is no
quality rating.
Manu-
facturer
Brand Name in acc.
with DIN 51825
Agip Agip GR MU3 K3K-20
ARAL Aralub HL3 K3K-20
BP BP Energrease LS3 K3K-20
ESSO BEACON 3 K3N-30
Fuchs RENOLIT FWA 220 K3N-20
Klüber MICROLUBE GL 263 K3N-20
Mobil-Oil Mobilux 3 K3K-20
Shell Shell Alvania Grease R3 K3N-30
SKF SKF Grease LGMT3 K3K-30
If none of the above roller bearing lubricants are
available, we recommend using a multi-purpose lubri-
cant on lithium basis in any case, which corresponds
to one of the above DIN names.
The mixing of greases with different basic oils and
thickeners leads to reduced lubricating properties and
should therefore be avoided.
The table in Chapter 7.1.2.6 shows the allocation of
the pump sizes to the amount in grease per gram.
Relubrication period
The bearings must be relubricated each 4,000 operat-
ing hours.
Relubrication
Relubrication takes place via the lubricating nipple
(119) screwed into the bearing bracket (110). Con-
tinue regreasing until the old grease emerges from
the bearing cover (131). Scrape the old grease off.
7.1.2.3 Shaft sealing
Shaft sealing either takes place via a stuffing box or a
mechanical seal.
• Stuffing box
Possibly increased leaks on the stuffing box during
the first operating hours normally decrease on their
own during the warm-up time.
If necessary, slightly tighten the hexagon nuts (202)
on the gland (203).
Please observe that there has to be a slight leak on
the stuffing box. This dissipates the friction heat that
forms on the sealing surface.
If the leaking losses increase disproportionately and if
this cannot be reduced by slightly tightening the
hexagon nuts (202) several times, the packing rings
have lost their shape elasticity and must be replaced.
! Dismounting the old packing rings and clean-
ing the stuffing box casing
After relieving the pump from pressure and re-
moving the gland, you can take out the old pack-
ing rings. Use a packing puller with elastic shaft.
Afterwards, carefully clean the stuffing boxspace
and the drive shaft in the area of the packing
rings. Used-up drive shafts respectively shaft pro-
tection casings must be renewed (see disassem-
bly and assembly instructions).
! Installing the packing rings
As a rule, you may only install
packing rings that correspond to
the required operating conditions of the pump.
The dimensions and required number of pre-
pressed packing rings and ring cuts respectively
cut lengths are listed in the table in Chapter
7.1.2.6.
With cuts we recommend the straight vertical cut
to the shaft. In order to achieve a gap-free, paral-
lel position of the cutting ends when closing the
packing ring, the cutting angle should be approx.
20° to both cut ends (see figure 1).
Figure 1: Cutting packing rings
Pre-pressed packing rings or ring cuts have to be
carefully turned open axial and radial so that they can
just about be slid across the shaft. Bending the rings
may lead to damages.
When installing in the packing space, carefully rebend
the packing rings to ring shape. The cutting joints
have to be shifted by 90° here. Each ring has to be
slid into the Stuffing boxspace individually with the
cutting ends facing forward by means of the gland.
The sealing chamber ring or flushing ring have to be
installed sequentially.
You may never use pointed objects
for this work. Danger of damaging
the shaft and deforming the packing material!
! Start-up the stuffing box after re-packaging
The stuffing box may only be tightened slightly
prior to start-up. When starting the pump, 50 to
200 drops per minute are an admissible leakage
quantity.
During the warm-up process of approx. 30 min-
utes, adjust a minimum leakage of 2 to 20 drops
per minute by evenly tightening the gland (203)
step by step via the hexagon nuts (202).
The stuffing box temperature
may not rise abnormally during
this process. Approx. 20° to 60°C above the con-
veyor liquid temperature are admissible. In case
10
Series AE1L, AE.E, AE.N, AE.H, AE.V, AED1E, AED2N
Design ID, ZD
of a rapid rise in temperature, the gland must be
loosened immediately and the warm-up process
repeated. The leakage can be carried off via the
threaded boring located in the strip tank in the
bearing bracket.
Rule out damages to persons and the environment
through leakage of dangerous substances!
• Mechanical seal
Non-relieved mechanical seals in all material pairings
and designs are applied. The mechanical seal is
maintenance-free.
In case of heavy leaks due to wear and tear, you
have to exchange the mechanical seal (see disas-
sembly and assembly instructions).
As the running dry of the mechanical
seals must be avoided, the pump
may only be operated in filled state and, if provided,
with activated additional installations (see Chapter
6.1.2).
7.1.2.4 V- belt drive
See our maintenance instructions for V-belt operation
with tensioning device VM 706.0001, Identity No. 133
586.
7.1.2.5 Drive engines and (variable speed gear) drive
See the operating and maintenance instructions by
the manufacturers.