1. POLYMERS
POLYMERS :
A large molecule built up by small, simple chemical units.
PROPERTIES :
1. Melt Viscosity :
It is the measure of the rate at which chains can move relative to each other. The higher the molecular weight, greater the melt viscosity.
2. Yield Strength & Modulus :
Many polythenes have the yield strength below 2000lbf/sq.inch (i.e.14MPa)While the nylon may have the value of 12000lbh/sq.inch (83MPa).
3. Specific Gravity :
It is the mass per unit volume.
Amorphous hydrocarbon polymers generally have sp.gravity of 0.86-1.05.
Where large atoms are present e.g.chlorine atoms,the sp.gravity is higher,such as
PVC-1.4.
4. Impact Strength :
Familarity with a given plastic material under normal conditions of use leads to it being considered as either a brittle or a tough material.
Thus polystyrene, unmodified unplasticised PVC are brittle where as L.D.P.E. & plasticized PVC are tough.
PRINCIPLES OF THE PROCESSING OF THE PLASTICS :
A large part of polymer processing technology can be summed up in the statement : “Get the shape & then set the shape .”
Such objects can be shaped by the following general techniques :
1. Deformation of polymer melt either thermoplastic or thermosetting processes operating in this way include extrusion, injection moulding & calendaring and form in tonnage terms.
2. Deformation of the polymer in the rubbery state of importance in vacuum forming, pressure forming & warm forging techniques.
3. Deformation of a solution usually either by spreading or by extrusion as used in making cast film & certain synthetic fiber & filaments.
4. Deformation of a suspension.This is great importance with rubber latex &the other lattices & with the PVC paste.
5. Deformation of lower molecular weight polymer or polymer precursor such as in the casting of acrylic sheets & glass reinforced laminates.
6. Machining operations.
The first five of these techniques involve deformation & this has to be followed by some setting operation which stabillises the new shape.In the case of polymer melt deformation,this can be affected by cooling of thermoplastics & cross linking f thermosetting plastics and the similar can apply to deformation in the rubbery state.
MELT PROCESSING OF THERMO-PLATICS :
In order to realise the full potential of process, it is necessary to consider the following factors –
1. Hygroscopic behavior of polymer compound.
2. Granule characteristics.
3. Thermal properties that influence the melting of the polymer.
4. Thermal stability.
5. Flow properties.
6. Thermal properties that affect the cooling of polymer.
7. Crystallisation.
8. Orientation.
Hygroscopic Behavior :
It is essential that the polymer compounds shall be free of water & other low boiling solvents. A
small volume of water can generate steam which will trend to be trapped within the compound during
the production stage.This will expand on decompression of melt in latter stage of process leading to
voids in the finished product.Such voids ar sometimes flattened out through shear during the polymer
flow, leading to reflecting surfaces known as “mica marks”.
Sometimes the water may just be present on the surface of compound & easily removed.In the
other cases, water may be absorbed in the body of the polymer & long drying period is necessary.
Thus the higher processing temperature, the lower is the tolerable level of water in the
compound.Since higher temperature will generate higher volume of steam with a fixed mass of water.
Granule Characteristic :
All one time it was quietly common practice to extrude & mould granules of varring shapes &
size that had been obtained by breaking of sheet between rotating 7 stationary blades.It was subsequently
found that the use of granules of more regular shape & even size can lead to much higher throughput
rates of extruders & much more even heating and hence better control in flow properties in all the process.
Thermal properties influencing polymer melting :
Polymer compounds vary considerably in the amount of heat required to bring them up processing temperatures. These differences arises not so much as a result of differing processing temperatures but because of different specific heats. Crystalline polymers additionally have a latent heat of fusion of the crystalline structure which has to taken in to account.
The specific heat is independent of the temperature. It is therefore necessary to use an average
figure for the specific heat over the range from room temperature to the processing temperature.
Polymer Sp.
Gravity Sp.Heat
J/g°c Latent heat
J/g Avg.moulding temp. °c Total heat reqd. J/cm3
ABS 1.01 1.46 - 225 305
Polycarbonate 1.20 1.26 - 300 422
Polyeheylene 0.91-0.96 2.31 209 220-280 610-740
Polystyrene 1.05 1.34 - 200 250
PVC (unplasticised) 1.44 1.00 - 180 230
polypropylene 0.90 1.92 100 250 487
The heat for melting can be generated externally,in which case heat transfer distances should be kept to a minimum & a temperature distribution will depend on the thermal conductivity, or internally either by a high frequency heating process or by mechanical mechanical working can provide a significant contribution.
The amount of frictional heat generated increases with the rate of working & with the polymer viscosity.
Since the melt viscosity decreases with the increasing temperature,the rate of frictional heat decreases with increase of temperature once the polymer is in the molten state.
In some polymer processing, the frictional heat generated exceeds the total requirement.So that provision has to be made for cooling facilities around the main heating chamber, be it an extruder barrel or an injection moulding cylinder.
Thermal Stability :
Polymer vary inoromously in their thermal stability. Before attempting to process,any specific polymer compound, its thermal characteristics to be considered
Stability at elevated temperature in absence of oxygen; i.e. the period of heating at typical processing temperature.
Stability at elevated temperature in presence of oxygen.
If the product is unstable, how are the polymer properties affected?
What degradation products, if any are given off ?
Is degradation catalysed by any metals which could be present in the processing machinery?
Is degradation catalysed by any other material with which the polymer might come in the contact.
Some materials are able to withstand quite lengthy ‘thermal histories’ i.e.intensity (temperature ) & the duration of heating.
Polyethylene & polystyrene may reprocessed a number of times with little more than a slight decolouration & in case of polyethylene deterioration in electrical insulation properties.
But PVC requires incorporation of stabillisers & even may discolour and give off hydrochloric acid,later having a corrosive effect on many metals.
At the same time some metals have a catalytic effect on these polymers so that care has to be taken in construction of barrel,screw & the other metal parts liable to come in contact with the polymers.
SOME POLYMERS & THEIR SHORT FORMS IN DAILY USE :
PVC Polyvinyl chloride
FRLS Fire retardant low smoke
HFFR Halogen free flame retardant
LDPE Low density (high pressure) polyethylene
HDPE High density (Low pressure) polyethylene
XLPE Cross linked polyethylene
EPR Ethylene Propylene rubber
HEPR High modulus/grade Ethylene Propylene rubber
PP Polypropylene
PS Polystyrene
HIPS High Intensity Polystyrene
SOME PROCESSES OF POLYMERS :
EXTRUSION :
Material is pumped with the screw pump, through a die to give a product of constant cross-section.
INJECTION MOULDING :
Material is pumped by a screw pump to the front end of the injection cylinder with the screw moving to the rear in order to provide the space for the material, then the screw moves forward as the injecting the molten material into a relatively cool mould in which the material sets.
EXTRUSION BLOW MOULDING :
The extruder tube is inflated in the mould while still above softening point.
CALENDERING :
Softened material is flattened out into sheet between roles.
Most Common Materials in Pipe Systems :
• PE-Polyethylene
Characteristics:
• Ductile behaviour
• Widely available in extensive pipe grades
• Easy to handle – pellet form
• Easy to extrude
• Good possibilities for recycling
• Tolerant to broad working temperature range
• Flexible allowing coiling to reduce jointing in long runs
• Can be jointed by welding
• Material is bought in pellet form already compounded
• MDPE
• HDPE –80 -100
• Relatively highwall thickness’required for pressure
• PVC –Poly vinyl Chloride
Characteristics:
• Can show brittle behaviour
• Flexible compounding possibilities
• Pellet or powder form
• Corrosive
• Typically scrap is not re-used in pressure pipes
• Brittle when exposed to cold temperatures
• Rigid –cannot be coiled
• High strength –low wall thickness in relation to pressure
• Linear Oriented PVC –extremely high strength
• Difficult to test
• PP -Polypropylene
Characteristics:
• High end product
• Good resistance to temperature
• Pellet form
• Easy to handle
• Ductile material
• Excellent surface quality
• PB -Polybutylene
Characteristics:
• Requires cross linking
• Good resistance to temperature
• Pellet form
• Easy to handle
• Ductile material
• Excellent surface quality
POLYMERS :
A large molecule built up by small, simple chemical units.
PROPERTIES :
1. Melt Viscosity :
It is the measure of the rate at which chains can move relative to each other. The higher the molecular weight, greater the melt viscosity.
2. Yield Strength & Modulus :
Many polythenes have the yield strength below 2000lbf/sq.inch (i.e.14MPa)While the nylon may have the value of 12000lbh/sq.inch (83MPa).
3. Specific Gravity :
It is the mass per unit volume.
Amorphous hydrocarbon polymers generally have sp.gravity of 0.86-1.05.
Where large atoms are present e.g.chlorine atoms,the sp.gravity is higher,such as
PVC-1.4.
4. Impact Strength :
Familarity with a given plastic material under normal conditions of use leads to it being considered as either a brittle or a tough material.
Thus polystyrene, unmodified unplasticised PVC are brittle where as L.D.P.E. & plasticized PVC are tough.
PRINCIPLES OF THE PROCESSING OF THE PLASTICS :
A large part of polymer processing technology can be summed up in the statement : “Get the shape & then set the shape .”
Such objects can be shaped by the following general techniques :
1. Deformation of polymer melt either thermoplastic or thermosetting processes operating in this way include extrusion, injection moulding & calendaring and form in tonnage terms.
2. Deformation of the polymer in the rubbery state of importance in vacuum forming, pressure forming & warm forging techniques.
3. Deformation of a solution usually either by spreading or by extrusion as used in making cast film & certain synthetic fiber & filaments.
4. Deformation of a suspension.This is great importance with rubber latex &the other lattices & with the PVC paste.
5. Deformation of lower molecular weight polymer or polymer precursor such as in the casting of acrylic sheets & glass reinforced laminates.
6. Machining operations.
The first five of these techniques involve deformation & this has to be followed by some setting operation which stabillises the new shape.In the case of polymer melt deformation,this can be affected by cooling of thermoplastics & cross linking f thermosetting plastics and the similar can apply to deformation in the rubbery state.
MELT PROCESSING OF THERMO-PLATICS :
In order to realise the full potential of process, it is necessary to consider the following factors –
1. Hygroscopic behavior of polymer compound.
2. Granule characteristics.
3. Thermal properties that influence the melting of the polymer.
4. Thermal stability.
5. Flow properties.
6. Thermal properties that affect the cooling of polymer.
7. Crystallisation.
8. Orientation.
Hygroscopic Behavior :
It is essential that the polymer compounds shall be free of water & other low boiling solvents. A
small volume of water can generate steam which will trend to be trapped within the compound during
the production stage.This will expand on decompression of melt in latter stage of process leading to
voids in the finished product.Such voids ar sometimes flattened out through shear during the polymer
flow, leading to reflecting surfaces known as “mica marks”.
Sometimes the water may just be present on the surface of compound & easily removed.In the
other cases, water may be absorbed in the body of the polymer & long drying period is necessary.
Thus the higher processing temperature, the lower is the tolerable level of water in the
compound.Since higher temperature will generate higher volume of steam with a fixed mass of water.
Granule Characteristic :
All one time it was quietly common practice to extrude & mould granules of varring shapes &
size that had been obtained by breaking of sheet between rotating 7 stationary blades.It was subsequently
found that the use of granules of more regular shape & even size can lead to much higher throughput
rates of extruders & much more even heating and hence better control in flow properties in all the process.
Thermal properties influencing polymer melting :
Polymer compounds vary considerably in the amount of heat required to bring them up processing temperatures. These differences arises not so much as a result of differing processing temperatures but because of different specific heats. Crystalline polymers additionally have a latent heat of fusion of the crystalline structure which has to taken in to account.
The specific heat is independent of the temperature. It is therefore necessary to use an average
figure for the specific heat over the range from room temperature to the processing temperature.
Polymer Sp.
Gravity Sp.Heat
J/g°c Latent heat
J/g Avg.moulding temp. °c Total heat reqd. J/cm3
ABS 1.01 1.46 - 225 305
Polycarbonate 1.20 1.26 - 300 422
Polyeheylene 0.91-0.96 2.31 209 220-280 610-740
Polystyrene 1.05 1.34 - 200 250
PVC (unplasticised) 1.44 1.00 - 180 230
polypropylene 0.90 1.92 100 250 487
The heat for melting can be generated externally,in which case heat transfer distances should be kept to a minimum & a temperature distribution will depend on the thermal conductivity, or internally either by a high frequency heating process or by mechanical mechanical working can provide a significant contribution.
The amount of frictional heat generated increases with the rate of working & with the polymer viscosity.
Since the melt viscosity decreases with the increasing temperature,the rate of frictional heat decreases with increase of temperature once the polymer is in the molten state.
In some polymer processing, the frictional heat generated exceeds the total requirement.So that provision has to be made for cooling facilities around the main heating chamber, be it an extruder barrel or an injection moulding cylinder.
Thermal Stability :
Polymer vary inoromously in their thermal stability. Before attempting to process,any specific polymer compound, its thermal characteristics to be considered
Stability at elevated temperature in absence of oxygen; i.e. the period of heating at typical processing temperature.
Stability at elevated temperature in presence of oxygen.
If the product is unstable, how are the polymer properties affected?
What degradation products, if any are given off ?
Is degradation catalysed by any metals which could be present in the processing machinery?
Is degradation catalysed by any other material with which the polymer might come in the contact.
Some materials are able to withstand quite lengthy ‘thermal histories’ i.e.intensity (temperature ) & the duration of heating.
Polyethylene & polystyrene may reprocessed a number of times with little more than a slight decolouration & in case of polyethylene deterioration in electrical insulation properties.
But PVC requires incorporation of stabillisers & even may discolour and give off hydrochloric acid,later having a corrosive effect on many metals.
At the same time some metals have a catalytic effect on these polymers so that care has to be taken in construction of barrel,screw & the other metal parts liable to come in contact with the polymers.
SOME POLYMERS & THEIR SHORT FORMS IN DAILY USE :
PVC Polyvinyl chloride
FRLS Fire retardant low smoke
HFFR Halogen free flame retardant
LDPE Low density (high pressure) polyethylene
HDPE High density (Low pressure) polyethylene
XLPE Cross linked polyethylene
EPR Ethylene Propylene rubber
HEPR High modulus/grade Ethylene Propylene rubber
PP Polypropylene
PS Polystyrene
HIPS High Intensity Polystyrene
SOME PROCESSES OF POLYMERS :
EXTRUSION :
Material is pumped with the screw pump, through a die to give a product of constant cross-section.
INJECTION MOULDING :
Material is pumped by a screw pump to the front end of the injection cylinder with the screw moving to the rear in order to provide the space for the material, then the screw moves forward as the injecting the molten material into a relatively cool mould in which the material sets.
EXTRUSION BLOW MOULDING :
The extruder tube is inflated in the mould while still above softening point.
CALENDERING :
Softened material is flattened out into sheet between roles.
Most Common Materials in Pipe Systems :
• PE-Polyethylene
Characteristics:
• Ductile behaviour
• Widely available in extensive pipe grades
• Easy to handle – pellet form
• Easy to extrude
• Good possibilities for recycling
• Tolerant to broad working temperature range
• Flexible allowing coiling to reduce jointing in long runs
• Can be jointed by welding
• Material is bought in pellet form already compounded
• MDPE
• HDPE –80 -100
• Relatively highwall thickness’required for pressure
• PVC –Poly vinyl Chloride
Characteristics:
• Can show brittle behaviour
• Flexible compounding possibilities
• Pellet or powder form
• Corrosive
• Typically scrap is not re-used in pressure pipes
• Brittle when exposed to cold temperatures
• Rigid –cannot be coiled
• High strength –low wall thickness in relation to pressure
• Linear Oriented PVC –extremely high strength
• Difficult to test
• PP -Polypropylene
Characteristics:
• High end product
• Good resistance to temperature
• Pellet form
• Easy to handle
• Ductile material
• Excellent surface quality
• PB -Polybutylene
Characteristics:
• Requires cross linking
• Good resistance to temperature
• Pellet form
• Easy to handle
• Ductile material
• Excellent surface quality