Site : Palm Oil Refinery
Unloading : From Truck Tanker to Storage Tanks
Loading Or Despatch Pump : from Storage Tanks to Truck Tanker
In a typical Palm Oil Refinery in Malaysia . the pumps are usually located about 3 to 5 meter
away from Trucks , and the storage tanks are located about 200 Meter or more away from ths pumping station
For unloading , normally no problem
If the same pumps are to be used for pumping from stoarge tank to the truck tanker ,with a
suction line of 200 M or more , problem such as cavitation will arise due to NPSH avialable being too low
Possibly when the tank level is high ,the pump may still work depending on the NPSH condition
When the level gets low ,serious cavitation occurs and this cause high reduction in flow ,pump noisy
and pump life gets shorten
Should there be intention for the pumps to be used both ways , the piping system must be designed to
suit the purpose ,that is taking into account the NPSH available for flow in both directions
23.12.10
27.11.10
STEP TOWADS INSTALLATION OF PUMPS
INSTALLATION & FOUNDATION
1.1 Pumpsets must be propoerly installed,make sure the concrete is stable even and rigid
1.2 Pump Piping should be properly supported independantly and lined up accurately with
the pump ports
Warning : never draw piping into place by force at the port connection of the pumps, severe
internal damages may result
1.3 Strainer of adquate size need to be selected and installed
1.4 Pump sets must be aligned
1,5 Instal flexible joints , vibration mounting pad etc
1,6 check rotation before starting the pump
1.1 Pumpsets must be propoerly installed,make sure the concrete is stable even and rigid
1.2 Pump Piping should be properly supported independantly and lined up accurately with
the pump ports
Warning : never draw piping into place by force at the port connection of the pumps, severe
internal damages may result
1.3 Strainer of adquate size need to be selected and installed
1.4 Pump sets must be aligned
1,5 Instal flexible joints , vibration mounting pad etc
1,6 check rotation before starting the pump
NOISE LEVELS - ELECTRIC MOTOR
The Data in the table below represents average test values .It is intended to serve as a guide in matters concerning noise and applies with a tolerance of +/- 3 dB(A)
Motor Frame
size 3000rpm 1450 rpm
rpm
63 53 41
71 59 45
80 60 49
90 65 54
100 69 58
112 64 58
132 69 60
160 72 62
180 73 64
200 72 63
225 74 67
250 74 67
Sound Level under no load
Souce of information : ABB Motor
Motor Frame
size 3000rpm 1450 rpm
rpm
63 53 41
71 59 45
80 60 49
90 65 54
100 69 58
112 64 58
132 69 60
160 72 62
180 73 64
200 72 63
225 74 67
250 74 67
Sound Level under no load
Souce of information : ABB Motor
23.11.10
SOUND LEVEL - IMO SCREW PUMP (ACG 045 . 052, 060 .070 )
Typical Pump Sound levels referred to free field conditions at a distance of 1 meter from the pumps.
Noise of driver Excluded in the quoted figures . The sound levels are measured at a discharge level of
5 bar 2900 rpm ,Viscostiy 37mm2/s
Model Connection dB(A)
045 50 mm 59
052 65mm 63
060 80mm 66
068 100mm 68
Noise of driver Excluded in the quoted figures . The sound levels are measured at a discharge level of
5 bar 2900 rpm ,Viscostiy 37mm2/s
Model Connection dB(A)
045 50 mm 59
052 65mm 63
060 80mm 66
068 100mm 68
22.11.10
Noise Level in Pumps
Various contributing factors that will produce noises when the pumps are in operation, such as the following
Mechanical Failures
a)Misaligned Pumpsets such as
- coupling misalignment
- Pipework misalignment at suction / discharge
- uneven concrete base
b )Bearing Problems
c) pump Problems, damaged by foreign material such as welding fluxes,bolts
or metals entering the pump
d) Isolators or Vibration Mounting Pad Not installed
e) Flexible Bellows not installed
Hydraulic Failures
a) Caviatation , NPSH avialable lower than required by the pump
b) Insufficient flow reaching the pump , this is most common as most installer fail
to determine the flow capacity of the pipe , ideal pipe diameter should be 80 mm
for 450 Lpm or 27 m3/hr ( quick calculation , pipe velocity can be found in earlier posting)
A very recent case , customer upgraded pump capacity from 200 lpm to 450 lpm
Previous suction line and tank outlet was 50 mm
However for this new installation, the tank outlet and suction line remained 50mm
Discharge product goes close to the outlet of the tank , creating air pockets which get into
the pump causing Noises
Othe Factors
a) Pump & Driver Size
b) Operating Pressure
c) Pump operating speed
For Cavitation cases , the following could be done or rectified
a) Reduce flowrate by reducing speed of pump
b) enlarge suction line
c) increase product level in the tank
d) avoid air pockets going the tank bottom and into the suction line
Sound Level complying to manufacturer should be acceptable
Mechanical Failures
a)Misaligned Pumpsets such as
- coupling misalignment
- Pipework misalignment at suction / discharge
- uneven concrete base
b )Bearing Problems
c) pump Problems, damaged by foreign material such as welding fluxes,bolts
or metals entering the pump
d) Isolators or Vibration Mounting Pad Not installed
e) Flexible Bellows not installed
Hydraulic Failures
a) Caviatation , NPSH avialable lower than required by the pump
b) Insufficient flow reaching the pump , this is most common as most installer fail
to determine the flow capacity of the pipe , ideal pipe diameter should be 80 mm
for 450 Lpm or 27 m3/hr ( quick calculation , pipe velocity can be found in earlier posting)
A very recent case , customer upgraded pump capacity from 200 lpm to 450 lpm
Previous suction line and tank outlet was 50 mm
However for this new installation, the tank outlet and suction line remained 50mm
Discharge product goes close to the outlet of the tank , creating air pockets which get into
the pump causing Noises
Othe Factors
a) Pump & Driver Size
b) Operating Pressure
c) Pump operating speed
For Cavitation cases , the following could be done or rectified
a) Reduce flowrate by reducing speed of pump
b) enlarge suction line
c) increase product level in the tank
d) avoid air pockets going the tank bottom and into the suction line
Sound Level complying to manufacturer should be acceptable
20.11.10
Pumps for Deioned Water
Recently came across a Food Mfr with HACCP ,using pumps of Cast Iron Construction whereas piping system is in Stainless Steel
Is this right or engineer simply dont realise ?
If the pump is for pumping raw water to Deionised System , not too bad but still , we are giving unnecessary extra load to the filters in the system, with rust ,extra
And if , the pump is for treated or Deionised Water ,then you are contaminating the water again
As the system builder has installed the cast iron pump , the user just follow the same replacment
without giving a thought
We do highlight , that stainless steel pump should be used
What he said ? Expensive
And this happened despite Inspector from relevant food department audited the plant
Is this right or engineer simply dont realise ?
If the pump is for pumping raw water to Deionised System , not too bad but still , we are giving unnecessary extra load to the filters in the system, with rust ,extra
And if , the pump is for treated or Deionised Water ,then you are contaminating the water again
As the system builder has installed the cast iron pump , the user just follow the same replacment
without giving a thought
We do highlight , that stainless steel pump should be used
What he said ? Expensive
And this happened despite Inspector from relevant food department audited the plant
27.8.10
AMK OPEN IMPELLER PUMPS
AMK SERIES
OPEN IMPELLER
MATERIAL IS SS 304 OR SS316
PUMP SIZE , 3X 2 , 4 X 3 , 6 X 4
SOLID SIZE : MAX 30MM
SOLID CONTENT : MAX 30 %
SHAFT SIZE : 1 1 /2 '' FOR ALL PUMPS
SHAFT SEALING :MECHSEAL -SILICONE CARBIDE
BEARINGS : DOUBLE BEARING FOR DRIVEN END
OIL BATH LUBRICATION
APPLICATION : CHEMICAL . EFFLEUNT .SLUDGE , WASTE TREATMENT
FOR HIGH CORROSIVE MEDIA , DRIP PAN BELOW STUFFING BOX IS PROVIDED SO THAT THE CHEMICALS WILL LEAK ON THE CAST IRON BEARING BRACKET OF THE PUMP
EXTERNAL WATER FLUSH IS PROVIDED FOR THICK SLURRY APPLICATION
JACKETED (HOT WATER OR STEAM ) ARE AVIALABLE FOR PRODUCTS THAT NEED HEATING UP , SUCH AS STEARIN . CPO ETC
STEAM TRACING IS NOT EFFICIENT AND SLOW TO HEAT UP
PALM OIL MILL - TREATED EFFLUENT LAND DISPOSAL OR COMPOSITE
Dear Zainuddin
As per your request , submersible pump is applicable for this job but take note as follow
a) pump impeller has to be non clog design, as the effluent will contain high solids and the solid content
depend very much on which location of the pond you locate the pump
b) Submersible pumps are centirfugal pmps , and flow will dropped sharply if the discharge pressure
increased , the Pipe is likely to be clogged due to scaling after sometime
c) if you are pumping about 1000kilometers away , need to work out the discharge pressure in the system carefully or you may no discharge at the end
d) Two stage Progessive cavity pumps will be most suitable as it can handle higher solid content, positive displacement and max pressure of 12 bar
e) as this is not a production pumps , dont go for too big or oversize capacity as bigger pump means not only paying more for the pump but also higher maintenace spares . A capacity of 40 to 60 m3 hr should be ideal
As per your request , submersible pump is applicable for this job but take note as follow
a) pump impeller has to be non clog design, as the effluent will contain high solids and the solid content
depend very much on which location of the pond you locate the pump
b) Submersible pumps are centirfugal pmps , and flow will dropped sharply if the discharge pressure
increased , the Pipe is likely to be clogged due to scaling after sometime
c) if you are pumping about 1000kilometers away , need to work out the discharge pressure in the system carefully or you may no discharge at the end
d) Two stage Progessive cavity pumps will be most suitable as it can handle higher solid content, positive displacement and max pressure of 12 bar
e) as this is not a production pumps , dont go for too big or oversize capacity as bigger pump means not only paying more for the pump but also higher maintenace spares . A capacity of 40 to 60 m3 hr should be ideal
COOLANT PUMPS -CNC MACHINE
Recently came across a CNC machine running with small amount of coolant discharge from the pump
Checked and found
a) Pump is too small , only about the size of a coffee cup and how much the flow we can expect ?
b) pump running on wrong rotation
c) although it may seem ro be alright , but lack of coolant accelerate the wear and damages of the tools
and these tools can be expensive
The point here , is machine makers or users failed to understand " quantity or flow in case " must be
right in any application
Suggestion : since there are few discharge nozzles around the millling tools and only one nozzle is discharging
coolant .the pump is definitely undersize .Determine the flow required from the manual or from
the pump at another machine which is big and performing . Replace the pump
Checked and found
a) Pump is too small , only about the size of a coffee cup and how much the flow we can expect ?
b) pump running on wrong rotation
c) although it may seem ro be alright , but lack of coolant accelerate the wear and damages of the tools
and these tools can be expensive
The point here , is machine makers or users failed to understand " quantity or flow in case " must be
right in any application
Suggestion : since there are few discharge nozzles around the millling tools and only one nozzle is discharging
coolant .the pump is definitely undersize .Determine the flow required from the manual or from
the pump at another machine which is big and performing . Replace the pump
Earlier Postings
FOR COMMENTS ON PUMP SELECTION SIZING AND OTHER INFORMATIONS , PLEASE LOOK AT EARLIER POSTINGS
THANK YOU
THANK YOU
13.5.10
USED FIREFIGHTING PUMP ( FOR SALE )
Dear All
One set of Firefighting Pump Model : EBSRAY 80-20 complete with 52 Hp Diesel
Engine in Tip Top Condition
One set of Firefighting Pump Model : EBSRAY 80-20 complete with 52 Hp Diesel
Engine in Tip Top Condition
26.3.10
Recondition of Pumps - Coating
Pump sand blasted Ready for coating and surface
preparation done according to
ISP 8501-01-ST3
Pump ready coated with Jotun coatings
Final Coat Alphatic Polyurethane
50 micron
Pump being undercoated before final coating
1st Coating with High Solid Epoxy 50 micron
31.1.10
Operating Cost of Pumps~ Energy
During the lifetime of a pump purchased , approximately 65 % of the cost goes to Energy , 5 % being the purchase cost of the pump and 35 % goes to maintenance & installation
Design the sytem head to optimum operating head, otherwise a bigger size pump and higher motor Kw is needed .
Result : higher maintenence and higher energy cost
Design the sytem head to optimum operating head, otherwise a bigger size pump and higher motor Kw is needed .
Result : higher maintenence and higher energy cost
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