Understanding Selection of Injection Moulding Machine.
Technological Solutions for Quality in Injection Moulding of Plastics
Technological Tools for Part Design, Mould Design & Mould Fabrication.
Plastic Injection Moulding process demands precise control of
It is found that different polymers have different characteristics and
different limitations in processing. Shear rate and shear stress influence
melt temperature, viscosity, density and flow behavior of polymer. Some
polymers are hygroscopic, some polymer have limited thermally stable time
which is different at different temperature. Such polymers have limited
residence time. The changes in each parameter has its own influences on
other parameters. Hence, process control becomes very intricate. This
calls for critical analysis of the machine specifications and
capabilities while ordering the machine.
To understand |
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calculation of max. shot weight for a material. |
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dependance of quality of melt for consistancy of moulding. |
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how it ensurs melt to spread through out when in fluid condition- before it freezes. Its relationship with freezing time. |
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how it overcomes resistance to flow during filling & pressure phase on account of flowratio & viscosity. |
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how it takes care of difficulty in fiiling for thiner walled and high flow ratio parts. |
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how it influences cycle time. |
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To understand |
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how it accomodates mould. |
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its significance for ejection of deep parts. |
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its relationship with mould open stroke and daylight. |
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its dependance on cavity pressure and method to compute cavity pressure. |
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HYDROMOTOR |
To ubderstand |
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torque requirement for -viscosity of- melt. |
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DRIVE POWER |
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Power supply frquency 60 or 50 Hz. |
its influence on speeds. |
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Pump-motor rating. kW |
to match the application - usage of machine. |
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CONTROLS |
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NO LOAD CYCLE TIME |
It indicates the time for non processing part of the cycle time |
This paper also discusses the following topics.
The shot weight of the mould (part & runner system) should be lower than the maximum shot weight of the machine for a given polymer. The maximum shot weight of the polymer can be determined by multiplying the density of polymer at moulding temperature by the maximum swept volume (in cc) of the machine. The characteristic of specific volume (cc/g) v/s temperature should be referred to obtain the density at moulding temperature. (Refer table)
The shear sensitive polymers like CA, POM, PMMA, PPO, PA, PBT, RPVC,, SAN etc have limited permissible residence time. It may be observed that
If total volume of screw channels = K x Max. shot volume then K x Max. shot weight (Volume)of m/c Residence time = --------------------------------------------------------------- x cycle time Actual shot weight (Volume) of mould time
(where K is a constant dependent on screw geometry)
K x Cycle Time x 100 Residence time= ------------------------------------------------------------------------ Percentage Utilisation of Injection Capacity
Higher percentage utilisation of injection capacity can reduce the residence time thereby maintaining it well below the permissible level.
Therefore, if the cycle time is estimated and permissible residence time for the polymer is known then.
K x cycle time x 100 Min.% utilisation of injection capacity =------------------------- -------------- permissible residence time
Therefore actual %age utilisation of injection capacity should be more than minimum % utilisation.
Permissible residence time has to be lower than thermal stability time.
TOPMaximum metering stroke available on the machine and percentage utilisation of maximum shot volume of the machine has important influence on processing and quality of moulded parts.
In 1980s the metering stroke used to be around 3.5 to 3.75 of screw diameter i.e s:D ratio. By 1987 the s:D ratio increased to 4.2. Now Italian machines have even higher ratio of over 4.5. Even higher ratio are also available. Higher ratio is not helpful in processing. Streaks and air bubbles appear on the moulding on account of excess s:D ratio.
It can be observed that effective screw length - from non return valve to the feed throat - decreases as the metering stroke increases. It is maximum (- as specified L/D ratio of 18 to 23 -) when screw tip is at fully forward position ( metering stroke is zero) and it becomes minimum when maximum metering stroke is reached.
The granules entering ( from feed throat ) the screw fall into the middle (approximately) of the feed zone at the end of metering stroke. These materials will obviously have to travel less to reach the nozzle through compression and metering zone. Whereas the materials entering the screw at the beginning of metering stroke - after injection stroke - have to travel longer path with in the screw to reach nozzle.
It means that amount of heat absorbed by the material due to conduction from heater and shearing in compression zone will not be constant but it will be varying from maximum to minimum. Therefore a temperature & viscosity gradient is introduced along the axis of the screw. This results in inhomogeneities in melt causing quality problem in moulded parts when metering stroke is more than 4D.
Therefore, inspite of available maximum shot volume corresponding to maximum stroke of say 4D or 4.5D, only maximum shot volume of 3D to 3.5D should be considered while selecting the machine. The following formula can be used to convert the stated shot weight to applicable shot weight.
Applicable shot weight = ( 3 / s:D ) . Stated shot weight
Injection time is related to injection rate (cc/sec.) and injection rate should be high enough to avoid freezing of melt during filling phase. Higher injection rate does not affect the thermally stable commodity polymers like HDPE, LDPE, LLDPE, PP, PS ect. The higher injection rate can be limited on account of sensitivity of polymer to shearing while passing through narrow passages (especially for engineering polymers). Freezing time is proportional to cube of minimum wall thickness. Generally injection time is also proportional to square of wall thickness.
TOPModgrn injection moulding machines are equipped with variable delivery or multiple pumps which are capable of delivering sufficient oil to injection hydraulic cylinder to give high enough injection speed for filling mould cavities rapidly.
Further, higher injection speed can be achieved by the use of hydraulic accumulator (normally offered as optional). Higher injection speed can push the melt to furthest part of mould at shorter time before the freezing of melt (increase in melt viscosity) on account of lower mould temperature.
During filling phase, injection speed is required to be under control with out disturbing the pressure setting. Therefore,set pressure has to be higher than actual pressure so that the relief valve is not actuated. On actuation of relief valve, there would be no control on injection speed. Thin walled commodity plastics items can be moulded with high injection speed.
Shear sensitive engineering polymers are likely to be overheated on account of excessive shearing due to high melt velocity. Hence, injection speed will have to be limited to suit the polymer characteristics. In modern machine injection speed can be set in multi stages - stroke controlled (up to 10 stages).
TOPThe injection pressure is required to overcome the resistance to flow of melt in the mould. It depends on melt viscosity,flow ratio and mould temperature. Set pressure is higher than actual pressure during filling phase. The relief valve is actuated on reaching set pressure during pressure phase. Higher injection pressure is required for processing high viscosity materials like PC, RPVC, TPU ect. At present new generation machines are capable of giving maximum injection pressure of 2200 bar or even 2500 bar.
Injection units are normally offered with the option of three screws (A, B & C) of different diameter.
A screw (lower dia) gives maximum injection pressure of around 1800 - 2400 bar.
B screw (medium dia) gives maximum injection pressure of around 1800 - 1500 bar with max. shot weight/volume higher than that of A.
C screw (higher dia) gives maximum injection pressure of around 1500 - 1300 bar with max. shot weight/volume higher than that of B.
Screw A is recommended for moulding
Screw B is recommended for moulding
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engineering parts of lower flow ratio with high viscosity polymer.·
commodity items of medium flow ratio with medium wall thickness in commodity polymer.Screw C is recommended for moulding
It should be noted that the maximum flow ratio of the part to be moulded should be lower than the maximum possible flow ratio of the polymer at the maximum injection pressure of the injection unit. Refer the table for maximum flow ratio of various polymer.
TOPMaximum linear injection speed in mm./ sec. decided by pump's flow rate and piston area of hydraulic injection cylinder.
Maximum linear speed mm/sec. = Flow rate of Pump / piston area of hyd. inj. cylinder.
Normally every machine manufacturer offers the option of 2 or 3 screws of different diameter. The injection unit is designed for a certain maximum injection power.
Max.Injection power ( Kg-cm. / sec) = Max. Injection Pressure x Max. Injection rate (cc / sec).
Therefore, maximum Injection power remains constant for 2 or 3 sizes of screw offered as optional with the Injection unit.
It should be noted that as diameter of screw increases, maximum rated injection pressure reduces and maximum injection rate increases. Screw's L/D ratio is normally designed for middle size of the three sizes of screw. Therefore, L/D ratio of lower diameter screw would be higher and higher diameter screw would be lower.
It should be realised that the biggest possible size of the item that can be moulded on a given platen area under a given clamp force from commodity plastics depends on maximum injection power available on a given injection unit.
It is the Injection power which is responsible for spreading the melt into the mould cavity. Lower powered injection unit can not be able to spread or move the melt to the boundary in all direction before melt looses its fluidity on account of continuous cooling of mould. As melt cools it looses it's fluidity and it's viscosity increases, thereby demanding more pressure and hence more clamp force and also more consumption of power. This results in moulded-in stress in the moulded part which is not desirable. Such parts fail due to stress cracking while in use.
TOPIt is the maximum rate at which polymer (Polystyrene) is plasticised. It is given in terms of Kg/hr or grams per second. The time taken to plasticise the given quantity of polymer can be calculated. It should be possible to complete the plasticising of shot weight within cooling time which can be estimated from the following formula .
Cooling time = Cc x (max. wall thickness mm)2
Cc = 3.5 to 5.5 for PS
1.9 to 4 for ABS
3.05 to 5 for POM
1.4 to 3.5 for PA6/6
2.0 to 4 for LDPE
The constant will also dependent on design of cooling channels in mould and it's effectiveness. In actual practice it will be more.
Latest machines provide screw rpm and reaction pressure settings (both) in 3 to 5 stages. It helps in improving precision of moulding.
TOPThe dimensions of shut mould should be such that it should be possible to pass through the clearance between tiebars and it should be possible to accommodate the mould on platen of the machine. Therefore, one dimension should be less than the clearance between tiebars and another dimension should be less than the platen size. Enough space should be made available to accommodate the clamps if direct bolting of mould on the platen is not provided.
The moulds should not be smaller than 0.7 times the clearance between tiebars. Smaller moulds if used at full clamping force are likely to give unfavorable platen deflection harmful for platen and tiebar life.
TOPThe shut mould height of the mould should be less than 1/3rd of maximum daylight so that there should be enough room for the ejection of part when mould platen is fully opened. If it is closer to 1/3rd of maximum daylight then the clearance between core and cavity of mould in fully open position should be verified on the drawing board.
The maximum daylight has to accommodate height of moving half of mould, height of moulded part, minimum and enough clearance for removal of moulded part and height of fixed half of mould.
With Hydraulic clamp machine, Maximum daylight = Minimum mould height + mould open stroke. If shut mould height is more than minimum mould height of machine then the mould open stroke is reduced to the extent of difference in shut mould height of mould and minimum mould height of machine. In case of Toggle machine, Maximum daylight = Maximum mould height + Mould open stroke. Mould open stroke remains constant in toggle machine.
TOPIt should be more than 2 or 2.5 times the part height so that there is enough room to remove the part.
TOPWith hydraulic clamp machine there can be only one specification of mimimum mould height. However, with toggle clamp machine, the shut mould height has to be between minimum mould height and maximum mould height of machine.
If the shut mould height is lower than the minimum mould height of the machine then the additional back plate of suitable thickness should be provided on the mould to build up the shut mould height equal to more than the minimum mould height of the machine.
TOPThe clamping force should be greater than the cavity force in the mould, i.e., mould opening force exerted by the melt in cavity. The cavity force depends on injection pressure and projected area of moulded part.
Injection pressure depends on maximum flow ratio of part and melt viscosity. The flow ratio of part depends on geometry of part and location of gate. Viscosity depends on characteristic of polymer.
It is necessary to calculate the following to determine cavity pressure.
where L1 = length of flow in section 1
T1 = wall thickness in section 1
and so on.
Clamping force > (cavity pressure) x (projected area)
The table gives the cavity pressure for a given flow ratio at a given wall thickness ( most predominant wall thickness). This table also gives the multiplication factor for different polymer melt.
FLOW RATIO |
W A |
L L |
T H |
I C |
K N |
E S |
S |
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L/T |
0.4 |
0.6 |
0.8 |
1.0 |
1.2 |
1.5 |
2.0 |
2.5 |
3.0 |
3.5 |
4.0 |
4.5 |
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bar |
bar |
bar |
bar |
bar |
bar |
bar |
bar |
bar |
bar |
bar |
bar |
75 : 1 |
400 |
320 |
270 |
220 |
180 |
180 |
180 |
180 |
180 |
180 |
180 |
180 |
100 : 1 |
480 |
400 |
340 |
280 |
250 |
190 |
180 |
180 |
180 |
180 |
180 |
180 |
150 : 1 |
720 |
570 |
470 |
420 |
370 |
320 |
220 |
180 |
180 |
180 |
180 |
180 |
200 : 1 |
900 |
750 |
700 |
570 |
500 |
410 |
320 |
250 |
220 |
180 |
180 |
180 |
250 : 1 |
1000 |
900 |
800 |
650 |
550 |
480 |
350 |
300 |
250 |
220 |
200 |
180 |
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Multiply the cavity pressure obtained from the above table by the following factors for different thermoplastics.
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HDPE, LDPE, PP |
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1.0 |
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Polyamide and styrene-butadien copolymers |
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1.2 - 1.4 |
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CA, ABS, STYRENE- ACRYLONITRILIE COPOLYMERS |
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1.3 - 1.5 |
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PMMA, mod PPO |
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1.5 - 1.7 |
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POLYCARBONATE,P V C |
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1.7 - 2.0 |
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Cavity pressure obtained from the above table when multyplied with the projected area gives the cavity force. The clamp force should be about 15% higher than the cavity force.
It can be observed that the largest portion of cycle time is cooling time which is proportional to square of maximum wall thickness and also efficiency of cooling set up. Therefore for faster production, wall thickness has to be low and efficiency of cooling system in mould as high as possible.
TOPThe option of high torque, medium torque and low torque hydromotor is now available. Normal (medium torque) hydromotor can be suitable for moulding most of the polymers with the exception of high viscosity polymer like PC, RPVC, PPO, TPU, etc. High viscous polymers need high torque hydromotor.
Low torque hydromotor can be recommended for the commodity plastics with thicker wall thickness. By adopting right type of hydromotor for specific application the melt at right temperature can be obtained and the power consumption can also be minimised.
TOPSince power is product of pressure (kg / cm 2 ) and rate (cc / sec.) actual power consumption is product of
and
through out the moulding cycle.
Peak of filling pressure and peak of injection rate do not reach simultaneously when wall thickness is large.
Peak of filling pressure and peak of injection rate may reach simultaneously when wall thickness is low, thereby demanding more power.
Lower wall thickness demands higher injection rate and the filling pressure can reach higher values when higher injection rate is in operation. Therefore, injection unit should have enough power rating to handle such moulding. This not being realised by many. They ignore injection rate specification of the new machine from Japan / Taiwan / Hongkong and find that they are not able to mould what was normally possible in SP series machine of same clamp force.
The POWER consumption is
To mould any part whatever power is required will have to be made available by the machine. However the energy efficiency deals with the reduction of wastage of power.
Hydraulic system provides dynamic power and heater control system provides thermal power. Efficiency of hydraulic system can be enhanced by using followings:
In our country power supply frequency is 50Hz. whereas, in many other countries like Japan, Taiwan, Hongkong, USA , etc. power supply frequency is 60Hz.
Prime mover for hydraulic pump is 3 phase Induction Motor whose RPM is directly proportional to frequency of supply and inversely proportional to number of poles of motor.
RPMs for different poles and Hz. given below:.
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SUPPLY FREQUENCY |
50 |
50 |
60 |
60 |
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Syn.RPM |
Actual RPM |
Syn.RPM |
Actual RPM |
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No. of Poles |
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4 |
1500 |
1440 |
1800 |
1728 |
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6 |
1000 |
960 |
1200 |
1150 |
It can now be observed that:
The size of the power unit is decided by plasticising rate and injection rate both having influence on quality and production rate. Fast cycling machine requires higher drive power.
Accumulator is used to increase the injection speed (rate) to enable parallel operations of ejector and core pull .
The option of three different drive power is possible
The connected power is decided by the power requirement for plasticising and injection. Moulding cycle has consist of 70% cooling time. 15 to 20% injection time and remaining 10 to 15% is taken up by mould close / open and ejection. During cooling time after dosing is over the machine is idling.
The power consumed during idling is normally 4 to 8% for Induction motor. This can be considered as power wasted. This wastage occurs during the balance period of cooling time after the plasticising is over. This wastage can be negligible if the cooling time is just enough for plasticising to be over.
The power wastage during idling is reduced by usage of multiple pumps which can be unloaded or loaded depending on the demand for power. The sequencing of loading and unloading is programmed in the software of microprocessor controls. The best energy efficiency is obtained by using variable delivery pump. Thus energy efficiency or less wastage of power depends on hydraulic system of the machine. This calls for evaluating hydraulic system.
The power consumed depends on product of actual pressure (read on pressure gauge and not set pressure) and injection speed. These parameters depend on geometry of part and viscosity of melt. If the connected power is lower than it may not be enough to fill larger parts of thin wall thickness (long flow ratio) even though the machine may have enough shot capacity. The lower connected power does not indicate lower consumption of power. It indicates lower capability for moulding bigger size of parts with large flow ratio. It defines the limitation of machine.
Low powered machine can enhance the injection power by incorporating hydraulic accumulator. This increases the cost of machine and also hassles of maintenance of accumulator.
TOPThe injections moulding machines with hydraulic clamp as well as toggle clamps are being manufactured in Europe, U.S., and Japan for last few decades.
Mould setting is quit simple in hydraulic clamp machine whereas in toggle clamp machine toggle mechanism is required to be shifted on the tie bars. Proper clamp adjustment demands more skill and judgment on the part of workmen. This is a very favourable advantage which user of both types of machines can confirm.
Maximum daylight as well as mould open stroke depends on toggle geometry whereas hydraulic clamp machine can be built easily for larger daylight by simply providing longer cylinder and longer tie bars. The longer mould open stroke can be provided by using longer clamp cylinder and ram. Therefor it is easier to satisfy special requirements of customers.
In hydraulic clamp machine
Mould open stroke = Maximum day-light minus Closed mould height.
Hydraulic clamp machines have enabled the moulders to set the mould easily by shifting the limit-switches. This feature has been liked by the users of machines.
In hydraulic clamp machine frictional resistance are encountered at
Therefore these seals have long operational life. It does not require any special lubricants. In-fact the hydraulic clamp does not require any attention and has always been proved more reliable.
There are eight toggle pins / bush joints in double toggle machines. Obviously wear-tear proportional to operational speed would take place at the joints as cent percent fail-safe lubricants are not available.
Since there are many machined parts in toggle any inaccuracies in these parts would result in mismatch of cylinder piston with cross head bore. This would result in unequal wear-tear of toggle pin / bush joints. It can also result in loss of parallelity between movable and stationary platens.
Mould close operation is carried out through small diameter bore cylinder and mould open operation is also carried out through the ram end of clamp cylinder. Equivalent cylinder is used in toggle machines to move the mould. Therefor to perform mould close / open operations oil requirement would be similar. The speed control is provided by hydraulic valves i.e. proportional valve or pressure compensated flow control valve in both types of machines. In spite of natural kinetics of toggle mechanism speed control in hydraulic system can not be eliminated.
FR series machine has such an excellent mould safety feature that mould close terminates and opens (about-turn) even if a paper is trapped between the mould. Therefore lack of natural kinetics is never felt in SP as well as FR machines.
In both the machines application of clamp force is against the deformation resistance of tie bars, mould and platen . In hydraulic machine the force is applied by a column of oil under pressure behind the ram of clamp cylinder. The oil is drawn in by gravity flow or sucked in during mould close operation. The oil column is pressurized by intensifier and the clamp force is retained by the non return / check valve with out consuming any additional power. The clamp force can be varied and set precisely at desired value by adjusting pressure switch or pressure control valve to suit the requirement of mould. The pressure intensifier has never posed any maintenance problem even after 7-10 years in SP series machines.
When toggle links are folded by pulling in of hydraulic cylinder, the mould is opened. Similarly when toggle links are straightened by pushing out of hydraulic cylinder, the mould is closed. The mould is clamped only when toggle unit is positioned in such a way so that in the fully straightened position of toggle links the two halves of mould meet. This alone does not confirm the clamping of the mould. Therefore special skill is required to adjust the position of toggle on the tie-bars so that mould is compressed slightly when the toggle links are fully stretched. Mould setting. therefore, is skill dependent job.
The toggle mechanism provides excess clamping force and "naturally" it can not be varied. To make clamp force variable or settable complicated and delicate strain measuring instrument with critical mechanism at high cost is required to be added. Even this is indirect measurement of clamp force which can not be accurate.
As the melt is injected (with speed) in to the cavity the cavity pressure steadily increases. At appropriate instant speed phase is terminated and pressure phase takes over. The injected melt expands in the cavity to reach peak pressure. This peak pressure multiplied by the projected area of mould cavity gives the force opposing the set clamp force. The cavity pressure drops as the melt cools in the cavity.
As long as the clamp force is equal to the peak cavity force both types of clamp system behave in the same manner .
However, as soon as the opposing force generated in the cavity exceeds the set value the behaviour of Toggle clamp and Hydraulic clamp differs.
In Hydraulic clamp unite the clamp force depends on the compressibility of hydraulic oil. Therefore rigidity of system need not be as high as in toggle clamp unit. Moreover if the cavity pressure increases it is indicated on the Tonnage indicator alerting the operator to search for the reasons in the process settings.
In Toggle clamp unit increase in clamp force, during peak pressure in cavity, depends on the rigidity of the mould and tie-bars of machine. A small expansion of the mould due to increase in it's temperature can increase stretching of the tie-bars and thereby increase the clamp force. A further expansion of mould can lead to breakage of tie bars. For these reason toggle clamps are designed for 10% higher clamp force.
TOPCycle time consists of
Mould open/close time can be determined by dry cycle time. It could be slowed down if the mould has moving/sliding parts. It should be noted that number of dry cycles per hr could be with or without movement of injection unit.
Injection time can be estimated by dividing shot weight by injection rate. Injection rate could be slower for shear sensitive material, and higher for commodity polymer.
25% to 35% of cooling time could be considered as follow-up pressure time.
Cooling time can be estimated by the following formula.
tc = cc x square of (max. wall thickness mm)
cc = 3.5-5.5 for PS
1.9-4 for ABS
3.05-5 for POM
1.4-3.5 for PA
2.0-4 for LDPE
Ejection time could be 3 - 6% of cycle time if the ejection is automatic.
For thermally sensitive polymer
permissible residence time x % utilisation of injection capacity cycle time <------------------------------------------------------------------------------------------------------- K x 100 where K is a constant dependent on screw geometry
There are no simple generalised formula for determining the injection time, injection speed and cooling time. The complex equations for these parameters can be solved by powerful computer with MOULD FLOW and MOULD COOL program. The constant of proportionality will be different at different set up (mould design) for different polymer. Therefore to predict the power requirement and cycle time we should understand the followings.
Where L is flow path and T is wall thickness
You will appreciate that the pressure is required to push the melt in to the cavity. It is directly proportional to longest flow path and inversely proportional to wall thickness. The ratio of L/T for a given part is called flow ratio. The maximum possible flow ratio for a given polymer melt at maximum possible injection pressure (of the machine) depends on the viscosity characteristics of the polymer melt. The maximum flow ratio can be about 250.
The prospective buyer will have to evaluate the requirement of his market. A list of items to be moulded should be prepared. The items should be listed in ascending order of shot weight and mould dimensions. Thereafter each parts should be evaluated in the following steps.
Steps for selection of Injection Moulding Machine
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1. a) Part
b) Drg.No.
2. Polymer-grade / make
a) Max.flow ratio
b) Degradation Temp.
c) Thermal Stability
3. Overall Size (in mm)
a) L x W x H
b) or m x mm
4. No. of Cavity
5. Weight
a) Part Weight
b) Shot Weight
(incl.of runner)
6. Estimated Shut
Mould Size (mm)
L x W x H
7. Projected Area
mm 2 or cm 2
8. Max.flow ratio of
Part
9. Most prevailing wall in thickness (mm)
10. Estimated cavity
pressure (bar)
11. Estimated Clamping
Force (tons)
12. Recommend IMM Model
a) Clamping Unit
b) Injection Unit
13. Screw size m mm
a) Hydromotor
b) Nozzle
c) Pump Power
14. %age utilisation of injection shot capacity should be such that Residence time < Thermal stability
Wall thickness and flow ratio are very are important while evaluating the machine specification and cycle time. Therefore we can classify the parts -to be moulded - on the basis of wall thickness.
ITEMS |
POLYMER |
APPLICATION |
WALL THICKNESS |
FLOW RATIO |
POWER REQ |
Disposable cup |
PP, PS |
Packaging |
< 1 mm |
highest |
highest |
Disposable syringe |
PP |
Health care |
< 1mm |
highest |
highest |
House wares |
HDPE, PP, LDPE, PS |
Domestic use |
Bet 1 & 1.5 mm |
depends on size |
high or medium |
Pipe fittings |
RPVC, HDPE, PP |
Water connection |
> 2 mm |
depends on size |
medium or low |
Pipe fittings |
RPVC, HDPE, PP |
Sewervage connection |
> 2.5 mm |
depends on size |
low |
Crates Tray |
HDPE, PP PS |
Storage, transportation |
> 1.5 mm |
high |
high or medium |
Industrial parts |
ABS, PC, SAN, PA, PMMA, POM, PBT,etc. |
Engineering |
bet 1mm & 1.5 mm |
varying |
medium |
- Tiny items |
Delrin, PA |
Clock / meter parts, |
< 1 mm |
low or medium |
medium |
- handles |
CA, PP |
Tools & industrials |
> 5 mm |
low |
low |
- Housing |
ABS, PS, PP |
Appliances, Instruments, TV, Eletronics |
bet. 1 mm & 2 mm |
high |
medium |
Cellular Phone parts |
PC, PC/ABS, Mod.PPO |
Telecommunication items |
=< 1mm |
high |
high |
Laptop & Notebook computer parts |
PC, PC/ABS, Mod.PPO |
Computer parts |
=< 1mm |
high |
high |
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TOP
The buyers of INJECTION MOULDING MACHINE normally check Clamp force, Platen size, Clearance between Tie bars, Maximum shot weight and maximum daylight. They do not seem to understand significance of Maximum Injection rate.
It is observed that many machine manufacturers in Japan, Taiwan and Hongkong offer larger platen area for a given clamp force but offer low powered injection unit when compared to SP series of DGP Windsor. With such specification, it can not be taken for granted that machine can mould any item whose mould can be installed on the platen of the machine , even though there is enough maximum shot weight available. It means that there is mismatch of platen size and maximum Injection power. Large size of platen becomes superfluous and misleading.
With out realising significance of Injection Power, the buyer tends to compare two different makes of machines on the basis of clamp force alone. This is not correct. The comparison should be on the basis of moulding capability - maximum Injection Power.
If one compares on the basis of Maximum Injection Power, then it will be realised that much larger size (clamp force) machine of Japan / Taiwan/ Hongkong make is required to mould the items routinely moulded on SP series machines at present.
Such machines are to be DE- RATED while comparing the price or cost benefit ratio. Maximum Injection Power of the machines under consideration can be computed and its ratio with the existing machines - SP series - maximum Injection Power can be found out. If ratio is lower than 1. then it should be DE- RATED by that factor. It means that lower powered machine can mould largest possible part smaller by that ratio factor.
Many Italian machine manufacturers offer larger maximum injection stroke up to 7 times diameter of screw to increase the maximum shot weight of the machine. As explained earlier, maximum injection stroke can not be more than 4 times diameter of screw for screws of L / D ratio up to 21. If L/D ratio is more than maximum injection stroke can be up to 4.5 times the diameter of screw. The maximum swept volume of the machine with larger injection stroke should be DE- RATED to the value corresponding to 4 times diameter of the screw while comparing with other machines. This is because such larger stroke can not produce uniform and consistent quality of melt resulting in poor consistency of quality of moulded parts.
Utilisation of shot capacity of the machine depends on cycle time, residence time and the thermal stability of polymer used.
DE-RATING of the speeds up to 20% are required if the specification is based on 60 Hz power supply.
Against the advantage of harmonic movement of toggles the following disadvantages of toggles OFF-SETS the balance and HYDRAULIC clamp becomes more favourable.
Energy efficiency deals with reduction in wastage of power by using superior hydraulic system.
The power wastage during idling is reduced by usage of multiple pumps which can be unloaded or loaded depending on the demand for power. The sequencing of loading and unloading is programmed in the software of microprocessor controls. The best energy efficiency is obtained by using variable delivery pump. Thus energy efficiency or less wastage of power depends on hydraulic system of the machine. This calls for evaluating hydraulic system.
The power consumed depends on product of actual pressure (read on pressure gauge and not set pressure) and injection speed. These parameters depend on geometry of part and viscosity of melt. If the connected power is lower than it may not be enough to fill larger parts of thin wall thickness (long flow ratio) even though the machine may have enough shot capacity. The lower connected power does not indicate lower consumption of power. It indicates lower capability for moulding bigger size of parts with large flow ratio. It defines the limitation of machine.
Controls should be easily understood and more user friendly. It should produce excellent repeatability of parameters. The operation and setting of controls should be well explained in the manual in ENGLISH. Normally manuals from far east countries are not written properly. It is more misleading and confusing. Before buying the machine one should look at their machine manual. They can also provide Video cassette on the controls and trouble shooting.
With imported machines the Guarantee of replacement of part is not advantageous. Any free replacement of parts attract import duty and it will not be possible to clear the urgent replacement parts with out paying substantial amount and hassles of dealing with custom officials. Hence to avoid such situation, vulnerable parts like set of electronic PCBs should be made available along with the machine.
CUSTOMERS NEEDS AND VARIOUS DESIGN OPTION AVAILABLE IN THE MARKET
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CUSTOMER'S |
DESIGN OPTIONS |
REMARKS |
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REQUIREMENTS |
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Easy to set mould. Energy saving in clamp or Convenience of mould setting ? |
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Easy to set process & user friendly control. |
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Scope for minimising sink marks. |
Multi-steps Injection speed settings |
Part design should avoid sink mark |
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Scope for minimising weld line or shift of weld line? |
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Part design should consider the question of weld line position. |
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Scope for shot weight consistency. Scope for precise dosing. |
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Not to use more than 3D stroke for injection. |
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Graphics of process settings |
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Useful only for those who understand it. |
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Sufficient Injection rate |
Flow rate determines flow ratio. i.e size of the possible moldable part.
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High injection rate enables to mould large parts. |
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High plasticising rate |
This decides the minimum cooling time for commodity polymers. |
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Life of non return valve on screw |
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Largest moulding possible |
Usable stroke can not be more than 3D. Largest flow ratio depends on injection rate. |
Maximum shot weight of machine = Swept volume x Density at moulding temperature . |
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Scope for Shortest cycle time. |
Dry cycle per hour indicates the fastest possible mould close / open time. Actual cycle time depends on cooling time which is largest in any cycle time. |
Cooling time depends on design of cooling circuit of mould and flow rate of cooling medium. |
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Open loop or closed loop controls. Open loop can give good results. (Actually it is Part design, mould design which is responsible for quality.) |
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Parameters under closed loop should be listed. |
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Reliability of mechanical parts |
Tie bars / Toggle pins,/ Gear box / Hydraulic monoblock / Non return valve of screw. |
How reliable they are? |
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Reliability of Electrical parts |
Contactors, relays, pressure switch, transducer, |
How reliable they are? |
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Reliability of Electronic systems |
All PCBs, Temperature controllers, |
How reliable they are? |
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Reliability of Hydraulic system & energy efficiency. |
Fixed delivery or variable delivery pump, no. of proportional valves, Cartridge valves, Hydro motor |
How reliable they are? |
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The machine has to be totally leak-free of hydraulic oil. |
This depends on manufacturing system, procedures, Company standards of precision, design features etc. |
How reliable they are? |
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After sales services |
Well trained service engineers with knowledge and experience in mechanical / hydraulic / Electronics should be stationed / available. |
This is very essential and very important. |
Technological Solutions for Quality in Injection Moulding of Plastics
Technological Tools for Part Design, Mould Design & Mould Fabrication.
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