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1.   5 4 Particle Size  Sludge     1  The service life of a pump may be greatly shortened by pumping fluids that carry small  particles or sludge  Its service life is dependent on the concentration of the particles  its  size  and hardness     2  For particle concentration less than 5   particle size smaller than 50 um  and hardness  within 80 Hs  SSiC bearings may be used  However  a shorter than normal service life    can be expected   11    AM SERIES    off the power at once and remove the obstruction     Should foreign matter enter the pump  it may cause pump damage or failure  Turn       CAUTION    5 5 Minimum Flow  Our pump uses the pumped fluid as its cooling and lubricating system  A low flow rate  may result in increasingly high temperature within the pump  and increased radial and axial    force  thus  affecting the pump   s performance and service life  Please use Table 5 1 for the    recommended minimum flow rate   Table 5 1 Unit  l min    AM 10  AM 30 50    Note  The above data is based on water  For volatile or viscous fluids  consult your local distributor     Do not operate the pump with outlet valve shut off more than 1 minute  Long shut      off time will cause the inside to heat up and may damage the pump           CAUTION    6  Operating Procedure and Notes    6 1 Notes Prior to Starting the Pump    1  Check the motor   s power rating  including frequency  voltage and wiring     2  Recheck to make sure all the parts  flange  pump casing  base plate  etc   are
2.   Pump Head   10    6 4 Shutting Down the Pump    1  Close the outlet valve slowly to prevent damage to the pump  due to reverse fluid flow   water hammer      2  Shut off the pump  It should stop gradually  If not  check the interior of the pump for  problems     3  The pump should be checked periodically  If the pump is used in a cold operating  environment  relative to the fluid   s freezing point   the fluid may crystallize even if the  pump is shut down for a very short amount of time  To prevent crystallization  a drain  plug should be included in the piping system or a heating system could be used to    maintain the temperature during shutdown     7  Maintenance and Inspection    7 1 Daily Inspection  See Table 7 1    Table 7 1  Appearance  1  Check for oxidation or corrosion of the front casing  bracket  and base plate      Check for leakage of the pump and the piping system      Check the pump exterior for any physical damage such as corrosion  peeled  paint    Operation  1  Check for irregular sounds and vibrations      Check for any abnormal overheating on the surface of motor  three phase  current imbalance  bearing noise  and foreign objects blocking the vent of fan   etc      Check the in tank fluid levels and inlet outlet pressures      Check the power supply and motor loading      Check and test run backup pumps regularly to ensure they can function  properly when needed        7 2 Periodic Maintenance  The following items should be inspected quarterly  refer 
3.  Pump head too high 3  NPSHa too low  resulting in cavitation   1  High frequency vibration and noise   NPSHa too low  2  Fracturing of the bearing and thrust rings   resulting in cavitation 3  Decreased pump performance and low flow rate   4  Serious cases may result in dry running   anticipated 2  Decoupling of the magnetic drive   1  Motor overloading   Viscosity higher than anticipated  2  Decoupling of the magnetic drive   3  Decreased pump performance and reduced flow   1  Corrosion and cracking   Wrong pump material selected  2  Rapid corrosion and wearing of bearing   3  Corrosion of the O ring resulting in leakage         Q   aD   Sa        Q     p   a        e     gt     SS  m    gt   D    VW  OE  a 5  oa  DM     AN        _  Q   aB            Q     p       15    AM SERIES                   Abnormal Condition Possible Symptom and Effect Damage       Inlet pipe not submerged 1  Produce high frequency vibrations and noise   sufficiently into the fluid or air  2  Fracturing of the bearing and thrust rings   sucked into piping system 3  Reduced pump performance   4  Serious cases can lead to dry running           a 1  Reduced pump performance   Pun Ceh eae ee te 2  Serious cases can lead to dry running   i Improper suction  resulting  in low efficiency   e a a a aleve insufficient flow  cavitation or dry running     Fluids within pump leaks during shut down period   resulting in dry running when pump is restarted     Starting the pump without priming     Starting the pu
4.  es    9 Inlet Pressure Gauge F  10 Inlet Piping l E  11 Inlet Piping Support S ali UW  12  Vibration Damper 1911  5   oe 7      rn H omer eee  13 Filter   ae 4   0 01 0 02 slope  14 Inlet Tank  13   qo   UUW E E  15 Foot Valve 7 14 4 h e j   5s A a Z  VW      ZA Z  Fig  4 1  Fig  4 2  Bad Piping Designs ai  h    gt 0 5m    h   or   gt 1 5D  a i  oo D Diameter  gt 1 5D  al Sind    A Me x    F ae  Fig  4 3    AM SERIES          Items to Note      Suction condition must satisfy NPSHa gt NPSHr 0 5 m      Reduce inlet Head as much as possible  Use straight and short piping      The pipes should have adequate structural support and shouldn   t use  the pump as its primary support   see Fig  4 1      When designing supports  consider the effects of temperature changes  on the supports to avoid thermal stress    General   Inlet piping and connectors should be installed properly to prevent  requirements drawing in air      The piping system should not have upward bumps that may collect air   The inlet piping should also have a 0 01 0 02 slope increase towards  the pump   see Fig  4 2      There should not be any elbows for at least 5 times the pipe diameter  from the opening of the pump  The elbow closest to the pump opening  should be a long radial elbow      There should be at least a 1 5 diameter distance between the pipe inlet  and the closest tank wall to prevent circulation   see Fig  4 4      The submerge depth of the inlet should be at least 0 5m or at least  twice the pipe d
5.  premium   equipment and complying  with established rules and standards  The following   recommendations should also be implemented     1   Power frequency  voltage and capacity should strictly follow the motor   s specification  sheet and name plate     2  Please select the proper non fuse switch  NFB  according to the rated current of the  motor     3  When using the pump for outdoor applications  please make sure the switch is protected  from rain     4  Keep the electromagnetic contactor  MC  from a pump at a suitable distance  with a  clearly marked warning sign to avoid false starts     5  Tags at the end of wires  or diagram shown in the terminal box  and method of  connection are based on the number wires  phases   power voltage and mode of start    for the motor  Be sure to connect the power cable in accordance with name plate for the  9    AM SERIES    motor and the connection diagram in the terminal box   6  All wiring operations must be in strict compliance with National Electrical Code and  local regulations  Make sure to choose the correct wire size and fasten the locking    screws to the right torque to prevent loose connections     Table 4 1 Wire size    Min  wire size  Recommended   AM 10 30 50    Table 4 2 Terminal screw and tightening torque  Screw size   Tightening torque  Recommended     45 kgf cm  80 kgf cm  120 kgf cm    Table 4 3 Recommendations for Grounding Wire       Cross sectional area of copper phase  Minimum cross sectional area of the  conduct
6.  securely  fastened     3  Fill the pump with liquid  priming  to remove any air within the pump and suction  piping     4  Check to ensure the inlet valve is open      5  Using a screwdriver  rotate the motor   s cooling fan to ensure it is not too tight or stuck     6 2 Starting Up the Pump    1  Check the direction of rotation of the motor by rapidly switching on and off the power     2  Direction of motor rotation can be checked from the fan side  It should be clockwise  seeing from the fan cover  follow arrow direction on the fan cover   If the rotating  direction reverses  change wiring phases by switching any two wire connections     3   Close the outlet valve and start up the pump     4  Slowly open the outlet valve when the motor has reached a stable speed  Adjust the  outlet valve to obtain the desired operating pressure or flow rate    6 3 Operating the Pump    1  Shut down the pump immediately in the case of cavitation or dry running     2  If decoupling should happen  shut down the pump to prevent reducing the magnet   s  strength    12    AM SERIES           3  During power outages  shut off the pump   s power supply and close the outlet valve     4  When switching on the pump with the outlet valve closed  the outlet pressure should  increase  If the pressure fails to rise  or if the pressure is too low  shut down the pump  and check the piping and wiring    NOTE  Outlet Pressure   Inlet Pressure   Pump Pressure   Pump Pressure  kg cm     Fluid Specific Gravity 
7. afaQ   iso 9007    Quality    afag    Environment    SERIES kgl    IECQ HSPM    MAGNETICALLY DRIVEN CHEMICAL PUMP       USER MANUAL                                                       S Aoo Ii       Symbols used    DANGER    AN    WARNING    CAUTION    Situation where improper handling or operation failure to follow this manual  would almost certainly result in death or serious bodily injury     Situation where improper handling or operation or failure to follow this manual  could result in serious bodily injury or death     Situation where improper handling or operation or failure to follow this manual  could result in bodily injury and or equipment damage     When pump is installed in an environment with a potentially explosive  atmosphere  strict adherence to our instructions must be followed  shown in this  manual with the Ex symbol   Situation where improper handling or operation or  failure to follow instructions in this manual would almost certainly result in  serious bodily injury or death        AM SERIES                Table of Contents       Foreword   2 Safety Requirements   3 Inspecting the Pump Prior to Installation  4 Installation  Piping and Wiring   5 Notes for Operation   6 Operating Procedure and Notes  7 Maintenance and Inspection   8  Incorrect Usage and Selection   9 Repair and Warranty   Annex A  Exploded View and Parts List    Annex B  Description of ATEX specific marking       AM SERIES    1  Foreword    Thank you for purchasing an ASSOMA pump  To e
8. aken when installing or storing the pump in the following  places  Please consult with ASSOMA INC  or authorized dealer in the near region   1  Places where flammable gas  dust or material is used or placed   CAUTION  2  Places where corrosive gas is generated   3  Places where the ambient temperature is higher than 40   C or lower than 0   C        4 2 Piping   1  AM 30 50 flange screw is either  M10 or 3 8     The tightening torque  is 5 N m    2  The allowable load of pipe on the  pump is as follows                                   Force  N  Moment  N m     Model    Fx   Fy      TaN   o  o  50   9   wo   is   wo   30    mo   100   80   so   40   25   4   25   o  mso   120   100   100   160  25   40   25  eo       AM SERIES    Model      mo   so   o  50   9   1   is     30    Note  The values in table are applicable for within 40   C       4 3 Notes for Installing the Piping System                                                                                                                                                                                                                                                                                                                                                                                                                                              1 Outlet Piping  2 Throttle Valve    3 Priming Piping y  4 Priming Valve  Lhe K  5 Check Valve 3 a Be  6 Outlet Pressure Gauge j   E35    _    7 Motor    x Z    6  8 Pump tt
9. ation   see Fig  4 4   2  The submerge depth of the inlet should be at least 0 5 m or at least  twice the pipe diameter below the liquid surface   see Fig  4 4   Inlet piping 3  There should be a distance of at least 1 5D between the bottom of the  tank and the beginning of the inlet pipe opening   see Fig  4 4   4 If there are two or more inlet piping in the same tank  they should be          placed at least 3D apart to prevent mutually disrupting each other   s  flow     Foot valve  Please install a foot valve if upward suction is used     1  If suction method is upward suction  please install a self priming           cylinder to prevent dry running due to a leaking foot valve   2  The size of the self priming cylinder should have a minimum liquid  level of at least 0 5 m above the opening of the pump       A control valve should be installed to make disassembling of the pump  easier  The valve should only be shut off when the pump is to be   Control valve detached for maintenance or repairs   2  We recommend the use of valves that have the least loss when fully    opened  like a gate valve       It is generally not recommended to install a filter in front of a pump   Filter which can unpredictably increase suction system resistance     If a filter has to be used  it should be cleaned regularly to ensure a    smooth flow   1 The material used should be corrosion resistant  otherwise  a pressure  gauge diaphragm should be used   2  During operation  if the vacuum gauge readi
10. cted power outages      A control valve can be used for controlling the flow of fluids  Do not  run the pump with the control valve closed for an extended period of  time     Control VALNE   When starting the pump  always start with a closed valve  and then    slowly open the valve to obtain the desired operating pressure and  flow  Always open or close the valve gradually     A vent should be installed if the horizontal section of the outlet piping is  Exhaust valve  very long     1  Suction condition must satisfy NPSHa gt NPSHr 0 5 m   2  Reduce inlet Head as much as possible  Use straight and short piping    3  The pipes should have adequate structural support and shouldn   t use  the pump as its primary support   see Fig  4 1    4  When designing supports  consider the effects of temperature changes       Ei on the supports to avoid thermal stress      General 5  Inlet piping and connectors should be installed properly to prevent  2 requirements sucking in air   see Fig  4 3    E 6  The piping system should not have upward bumps that may collect air     The inlet piping should also have a 0 01 0 02 slope increase towards  the pump   see Fig  4 2    7  There should not be any elbows for at least 5 times the pipe diameter  from the opening of the pump  The elbow closest to the pump opening  should be a long radial elbow        AM SERIES    Items to Note    1  There should be at least a 1 5 diameter distance between the pipe inlet  and the closest tank wall to prevent circul
11. d level    Low flow over extended period of  time           5  ao      D   F       a  D   s         Oua  z  pd               Damaged impeller    Damaged motor bearings       Wearing of the impeller bearings       Blockage of inlet piping or foot  valve    Improper Maintenance    Blockage of the outlet piping       AM SERIES    9  Repair and Warranty    When a problem arises  please read this instruction manual and try to troubleshoot the  problem  If the problem cannot be found  or if replacement parts are needed  please call the  distributor  and give them the following information     1  The pump model and manufacturing serial number indicated on the nameplate    2  The operating condition    3  The situation under which the pump fails     Please refer to the warranty card for details of the warranty terms and conditions     17    AM SERIES    Annex A  Exploded View and Parts List    Inlet Flange Impeller   Rear Thrust Ring  B21  M    B21   Bracket  Shaft Base  Motor                                        Table A  AM series tightening torque  Material    Item       18    AM SERIES    Annex B  Description of ATEX specific marking    1  The ATEX specific marking of pump body  without motor  is indicated on the name plate     2  Please check the name plate on the motor for ATEX specific marking for the motor     The ATEX specific marking indicated on the name plate of pump        x Il 2 G c HWA T4    Distinctive Community mark  Equipment group  2 Equipment category    Where ex
12. eeds 2 5 m sec  4  Two or more pumps share the same outlet piping system   5  To prevent back flow  water hammer  from damaging the pump during  unexpected power outages      A control valve can be used for controlling the flow of fluids  Do not  run the pump with the control valve closed for an extended period of  time     When starting the pump  always start with a closed valve  and then  slowly open the valve to obtain the desired operating pressure and  Control valve  flow  Always open or close the valve gradually     To facilitate the adjustment of discharge flow and the adjustment of  motor overload  it is recommended to install valves on outlet piping     And if both a check valve and a control valve are to be installed  the  order of allocation is pump     check valve     control valve     A vent should be installed if the horizontal section of the outlet piping is  Exhaust valve  very long     1  Explosive and inflammable liquids    2 Corrosive liquids    3  Toxic liquids    4  Liquids harmful to the human body or detrimental to health   5  Liquids that could produce a chemical reaction          Be cautions when dangerous liquids are transferred  When the pumps are used to     transfer dangerous liquids listed as below  the pump  piping and fittings must be  checked and monitored to ensure no leakage occurs  Leakage may result in   WARNING   personal injury  explosion  and or fire     4 4 Wiring  The wiring system should be done properly by qualified personnel  using
13. fan feels tight or if there are unusual sounds  the interior of the  pump may have been damaged during shipping    If there is any damage to the pump  please contact the seller immediately to arrange for  replacement parts  and to allow for timely communication with the logistics company  to determine liability    Each pump has a name plate  indicating the pump model  MFG number  rated head   flow rate  and motor power  voltage and frequency  Check these data to ensure they  comply with your order and application    Although some motors are marked usable for both 50 Hz and 60 Hz  the impeller size  of the pump should be trimmed according to frequency applied  Application under  incorrect frequency may cause motor overload  use under higher frequency  or pump  under performance  use under lower frequency     Name plate information  including motor name plate and pump name plate  plays an  important role for the operation and maintenance of the pump  It 1s proposed to re copy  data on nameplates and store it securely    The flow and head on the nameplate is the rated operating point or the operating point  based on customer demand  Where  Head  means  Total head      Total Head  Static Head   Dynamic Head    V   Vi    Total head  H     28    The pump is designed and manufactured to the specifications agreed upon by the  user and ASSOMA INC   such as fluid composition  fluid temperature  working  pressure  environmental conditions and necessary operational information  Use the  
14. fect certain medical devices  such as pacemakers   Personnel with such   devices are advised to consult their physician and device manufacturer to determine a   safe distance from the pump    The pump operator and pump operation supervisor must not allow any   operator who has little or no knowledge of the pump to run the pump  Pump   Operators must have a sound knowledge of the pump and its operation    Do not use a damaged pump  Doing so could result in injury or fire    Keep the pump away from heat source or direct flame  Do not place any open   flame or flammable object near the pump    Transport  installation  piping and wiring connections  operation  adjustment    maintenance and inspection should be carried out by qualified personnel    Having unqualified personnel perform these tasks could result in electric  CAUTION shock  injury or fire    Do not block name plate or warning labels from view    Do not stand on the pump or place heavy objects on the pump under any   circumstances  Failure to comply may result in equipment damage and or   serious injury    Disposal of used or damaged pump must be done in accordance with local   laws and regulations        AM SERIES    3  Inspecting the Pump Prior to Installation     1      2      3      4      5      6      7     Check the pump exterior for any physical damage that may have been incurred during  shipping    Use a small screwdriver to rotate the impeller of the motor   s cooling fan  The fan  should turn easily  If the 
15. iameter below the liquid surface   see Fig  4 4          op Inlet piping   There should be a distance of at least 1 5D between the bottom of the  2 tank and the beginning of the inlet pipe opening   see Fig  4 4    3   If there are two or more inlet piping in the same tank  they should be     placed at least 3D apart to prevent mutually disrupting each other   s    flow    Foot valve  Please install afoot valve if upward suction is used   see Fig  4 1     1  If suction method is upward suction  please install a self priming  Self priming cylinder to prevent dry running due to a leaking foot valve   cylinder 2  The size of the self priming cylinder should have a minimum liquid  level of at least 0 5 m above the opening of the pump     Acontrol valve should be installed to make disassembling of the pump  easier  The valve should only be shut off when the pump is to be  Control valve detached for maintenance or repairs     We recommend the use of valves that have the least loss when fully  opened  like a gate valve       It is generally not recommended to install a filter in front of a pump   Filter which can unpredictably increase suction system resistance     If a filter has to be used  it should be cleaned regularly to ensure a    smooth flow       The material used should be corrosion resistant  otherwise  a pressure  gauge diaphragm should be used   Vacuum gauge   a        During operation  if the vacuum gauge reading fluctuates  either there    are air bubbles in the syste
16. m or cavitation has occurred     AM SERIES          Items to Note      The weight of the outlet piping should be properly supported to prevent  putting excessive stress on the pump   see Fig  4 1     A priming piping must be installed if the suction system does not    General employ positive pressure  1 e  upward suction   see Fig  4 1   requirements   The flow rate in the outlet piping should not exceed 3 m sec     The ability for each component in the piping system to withstand  pressure should be calculated  to determine the maximum allowable  operating pressure     anaes Upward suction pumps that do not have a self priming cylinder should  S PIPIS Ihave a priming piping system       Pressure gauge used should be able to read beyond the maximum  operating pressure      Pressure gauge should be made of material that is corrosive resistant   otherwise a diaphragm should be used      A valve can be installed on the piping that leads to the pressure gauge   to facilitate maintenance and to lengthen the gauge   s service life      During operation  if the pressure gauge reading fluctuates  either there  are air bubbles in the system or cavitation has occurred          Pressure gauge    Outlet Piping    A check valve should be installed in the following situations     Discharge pressure exceeds 2 kg cm  and flow rate exceeds 3 m sec   Check valve   Two or more pumps share the same outletpiping system     To prevent back flow  water hammer  from damaging the pump during    unexpe
17. mp without priming   pump without prinung Diy running  causing damage to pump     direction  voltage    1  Low performance and vibrations due to drawing  in air      Fracturing of the bearing and thrust rings      Dry running      Produce vibrations and noise    Foreign objects stuck in impeller  2  Reduced efficiency and flow  Serious cases may  result in dry running      Insufficient cooling of pump      Excessive radial and axial force  reducing service  life of bearing and thrust rings    1  Low NPSHa  resulting in cavitation    Transfer fluid temperature too high  2  Reduced strength of the magnet  resulting in   decoupling     1  Rapid wearing of the bearing   Fluid cay ar aic les 2  Wearing of the impeller and casing surfaces     Deformation of the O ring Result in leakage  0 in Result in leakage  0    1  Resulting in vibrations and noise    2  Reduced pump performance and fluid flow   1  Produce vibrations and noise    2  Overloads the motor    3  High Motor temperature     Cooke Ae E off 1  Produce vibrations and noise   P 2  Overloads the motor     1  Produce vibrations and noise    2  May result in fracturing of the impeller shaft      Reduced pump performance and low flow rate or  may result in cavitation      Serious cases may result in dry running      Low flow or no flow      Pump unable to dissipate heat      Serious cases may result in overheating of the  pump and outlet piping    Improper Piping or    Leaking foot valve or inlet piping    Low inlet tank flui
18. ng fluctuates  either there  are air bubbles in the system or cavitation has occurred     The weight of the outlet piping should be properly supported to prevent  putting excessive stress on the pump    A priming piping must be installed if the suction system does not  employ positive pressure  1 e  upward suction     The flow rate in the outlet piping should not exceed 3 m sec     The ability for each component in the piping system to withstand  pressure should be calculated  to determine the maximum allowable  operating pressure     Self priming    cylinder       Vacuum gauge    General  requirements   see Fig  4 1     Co he ee Upward suction pumps that do not have a self priming cylinder should  eee oa  have a priming piping system     1  Pressure gauge used should be able to read beyond the maximum  operating pressure    2  Pressure gauge should be made of material that is corrosive resistant   otherwise a diaphragm should be used     Outlet Piping    lw s   3  A valve can be installed on the piping that leads to the pressure gauge     to facilitate maintenance and to lengthen the gauge   s service life   4  During operation  if the pressure gauge reading fluctuates  either there  are air bubbles in the system or cavitation has occurred        AM SERIES    Items to Note       A check valve should be installed in the following situations   1  Outlet piping is long   2  Head of outlet is more than 15 m   Check valve 3  Discharge pressure exceeds 1 5 kg cm  and flow rate exc
19. nsure proper operation and  maximum efficiency  please read this instruction manual carefully  Failure to follow the  recommended operating instructions outlined in this manual may result in serious personal    injuries and or equipment damage     2  Safety Requirements    This section lists general information about safety  The relevant safety requirements of  installation  wiring  operation and maintenance will set out in the relevant  sections   ASSOMA INC  may not be held responsible for personal loss or property damage resulting    from failure to follow the safety instructions contained herein     ACE certified motor should be used    The explosion proof grade of AM series pump is dependent on the material   selected and motor used  Please consult our order specification sheet or   contact one of our local representatives to  select the best product for your   needs  Refer to Annex B  for a description of the ATEX markings    Be sure to turn off the power before connecting  disconnecting or making any   changes to the pump   s wiring    The customer shall not modify the pump under any circumstances  Doing so   could result in an unexpected accident  ASSOMA INC  shall not be   responsible for accidents or damage resulting from equipment modified by the   customer    Be sure to take special precautions when performing operations if using   hazardous  explosive or inflammable liquids    Strong magnetic field warning  The AM pump uses strong permanent magnets   which may af
20. nternal parts     3  We recommend using a dry run protector to detect dry run occurrences to avoid    causing unnecessary damage to the pump     5 2 Operating Temperature    1  Operating temperature may change the fluid   s viscosity  vapor pressure  and  corrosiveness  Please ensure that your pump is operating within the proper temperature  range     2  The optimal temperature range for pumping pure water   Casing material PP PPG PVDF  0   C 80   C  Casing material ETFE CF  0  C 95   C    3  Please consult your local distributor for the temperature range suitable for your  chemicals      4  We recommend an operating environmental temperature to be between 0  C 40   C     piping with your bare hands  It may cause burns  Any exposed hot surfaces       including pumps  motors and piping  must have warning signs prominently displayed   CAUTION   The parts should be isolated from accidental contact     When the pump is used with a hot liquid  do not touch the front cover or the       5 3 Concentrations  Viscosity and Specific Gravity    1  Achange in a fluid   s concentration will usually affect its viscosity and specific gravity   Other physical properties like corrosiveness  may also change with the fluid   s  concentration  therefore  the selected pump material should be able to withstand the  corrosive properties of the fluid     2  When the fluid   s viscosity and or specific gravity differ from that of water  the shaft    power  flow rate and pump head may change as well   
21. ors supplying the equipment external protective copper conductors      Be sure not to performing any type of maintenance while the power is on  It  may lead to electric shock     Power supply and wire connecting work should be performed by qualified   DANGER personnel only      After wiring  be sure to replace the terminal box cover in its original position   Failure to do so could result in electrical shock      Install an earth leakage breaker  The operation of a pump without using an  earth leakage breaker may cause an electrical shock  Install an optional  leakage breaker in the system before running operation      The pump  should be properly grounded with a recommended ground  resistance of 10 Q or less   In Taiwan  use third type grounding      Each pump must have a separate grounding wire directly connected to the  common ground terminal  and must not form a loop between wires      If long wiring results in more than 3  voltage drop in the line  replace with  bigger gage wires     WARNING       10    AM SERIES    5  Notes for Operation  5 1 Dry Running     1  Our pump use the transfer fluid as its internal cooling system  therefore  dry running  the pump can cause the temperature to rise to a dangerous level that may seriously  damage the pump     2  If dry running occurs  switch off the pump immediately  Let it cool for at least an hour  before priming the pump to prepare it for normal operation  NOTE  Do not subject the  pump to rapid cooling  which may damage the i
22. plosive atmospheres caused by gases  vapors  or mists are  concerned     Protection type   Constructional safety    T4   Temperature class   Max  permissible surface temperature 135   C          a        cs  EI    1  When pump is installed in a potentially explosive atmosphere  be sure to select  an explosion proof motor  and  make sure both the pump and the motor are  suitably rated for the environment    DANGER   2  Both pump  and motor must be properly grounded  or there may be a risk of  static electric discharge    3  Never run pump without priming  Never operate the pump below the minimum  recommended flow rate for over   minute      gt              19    
23. pump strictly in accordance with the pump specifications and application range  If  the user intends to change the operation condition  please contact ASSOMA INC     or the authorized dealer in the near region to obtain the permission in writing  before operation    Unpack  a pump for inspection without proper hoisting  support or lifting  equipment may cause serious personal injury or damage to the pump        CAUTION    AM SERIES    4  Installation  Piping and Wiring    4 1 Installation Location    1  The pump should be close to the ground and located near the inlet tank     2  There should be sufficient space reserved around the pump to  facilitate future  maintenance and repairs     3  The pump and its wiring should be placed in a relatively dry environment  protected  from possible flooding     4  Install in a location where the ambient temperature will not rise above 40   C     5  Secure the pump to a level base plate or to equipment with anchor bolts     6  May not be used at altitudes above 1000 m     1  Be sure to use the hanger bolt  where applicable  to lift the pump  Lifting from  other parts of the pump may damage the pump  When hoisting  do not pass  under a raised pump  A serious injury could occur if the pump is accidentally   WARNING dropped     Before lifting  check the weight of the pump  Do not lift a pump which  exceeds the rated weight of the hoist  And  be sure no one is standing below    the pump while lifting or transporting   Special care should be t
24. s for the bearing and shaft  However  the    total wear between the shaft and bearing  bearing ID     shaft OD  must not exceed 0 3       Shaft sleeve outer diameter  AM 50    mm  Similarly  the total wear between the thrust ring and wear ring must not exceed 0 3  mm  When replacing the individual parts  you may choose to replace just the parts that    have more wear     7 4 Preventive Maintenance  Operational data  like vibration   flow rate  voltage  etc  can be collected   and upper and lower limits can be set  for each of the values  The collected  data can be used for trend analysis  see  Fig  7 1   which can be a basis in which  to determine when to carry out  preventive maintenance  e      Upper control   imit Time  AM 1s made at factory with LCL Lower contro  Limit  vibration below 3 0 mm   sec  rms  Fi  ig  7 1   measured at flange edge of bracket    and the noise value is below 75 dB  at  rated point      UCL    i       _     T    LCL    Measured Data         14    AM SERIES    Strong magnetic field warning  AM   s powerful permanent magnetic coupling  could adversely affect persons who are assisted by medical electronic devices  such as a pacemaker    DANGER   2  Be sure to turn the power off before performing any type of maintenance   repair or inspection  Make special provisions so that no other operator  mistakenly turns on the power supply while someone is working on the pump   In a noisy or poor visibility environment  display a sign near the power supply  swi
25. tch to notify others that someone is    WORKING    on the pump  Power  supply mistakenly turned on during maintenance may lead to personal injury   When handling chemicals  ventilate the work area well  In addition  the  operator must wear protector gear  such as a safety mask  safety goggles  and  protective gloves     No remodeling  Remodeling of the pump by the user may result in serious  injury  electric shock  or damage to the pump  Do not attempt to remodel as it  is very dangerous   Strong magnetic warning  The impeller assembly contains strong magnets  Be  careful not to get your hands or fingers pinched during assembly of the pump   Keep magnetic cards and electronic devices away from the pump to prevent  the magnetic field from causing damage       Use the right tools for any maintenance  disassembly or assembly        Be careful with hazardous liquids      If pumping dangerous chemicals  be sure to drain the pump before   CAUTION disassembling and rinse the parts and connecting pipes fittings well after  disassembly  Please note that small amounts of chemical may still remain in  the internal parts or pipe fittings        8  Incorrect Usage and Selection    Abnormal Condition Possible Symptom and Effect Damage    System resistance too high 1  Insufficient or no flow   or 2  Pump unable to effectively dissipate heat   Pump head too low 3  Excessive wear on bearing and thrust rings   Resistance lower than expected  1  Excessive flow   or 2  Overloading of the motor  
26. to Table 7 2    Table 7 2    Inspection Item    F  Cracks 1  Replace  2  Scratch marks  except when pumping 2  Contact the distributor    Front and Rear particle laden fluids     Casing    3  Crystallization or sludge 3  Clean  a      Shaft support loose or deformed 4  Contact distributor    O ring   Deformed  corroded or swollen Replace        SY    Impeller and 1  Scratch marks or cracks 1  Contact distributor  Magnet 2  Cracked bearing or crys vation 2  Contact distributor       AM SERIES          3  Bearing displays signs of wear and tear  3  Replace if worn excessively  4  Crystallization and other sludge  5  Foreign objects stuck in impeller 4  Clean  6  Impeller deformed 5  Remove the objects  6  Contact distributor    Shaft and Thrust  1  Scratch marks 1  Contact distributor  Ring 2  Cracks 2  Replace    1  Resistance of three phases and insulation  l  Repair or change if abnormal    impedance is found   2 Check amount of lubricant when using  2  Keep amount of lubricant at  open bearing  proper level     Used gasket or O ring  even without displaying sings of corrosion  may also  cause seal failure due to deformation or elastic reduction  We strongly  recommend replacing the O ring when the pump is under repair or service        CAUTION    7 3 Maintenance and wear tear limits  Table 7 3 Unit  mm    Shaft outer diameter     2 1 7  ree ee  AM 30 Bearing inner diameter   Thrust ring thickness    Thrust ring thickness    Note  Table 7 3 provides the recommended dimension
    
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