Higher Technological Institute-10th of Ramadan City
Department of Chemical Engineering
2018
Presented by Students
AbdAl-Rhman Magdy AbdullahYoussef
20160517
AbdAl-Rhman Ali Basheer
20160476
Amr Ahmed Saeed
20160629
Supervisors
Prof. Maher Gamal
Professor of Chemical Engineering
Department of Chemical Engineering
HigherTechnological Institute-10th of Ramadan City
Eng. MohammedYahiya
AssistantTeacher
Department of Chemical Engineering
HigherTechnological Institute-10th of Ramadan City
POLYCARBONATE
November
Contents
Introduction
✓ Polycarbonate or Lexan was discovered by;
Dr. Hermann Schell and his team at Bayar company in 1953.
✓ It is a condensation product of bisphenol A, and a carbonate
donner such as phosgene or diphenyl carbonate.
✓ Industrially it manufactured by;
❑ Interfacial polymerization (Bisphenol-A+Phosgene).
✓ It can be processed by Extrusion or Injection molding.
✓ Polycarbonate is a good engineering thermoplastic material having many good
optical, thermal, electrical and mechanical properties.
✓ It has many applications in different fields such as; electronics and automotive.
❑ Melt polymerization (Bisphenol-A+Di-Phenyl carbonate)
POLYCARBONATE
PROPERTIES
✓ A study of the molecular structure of bis-phenol A polycarbonates enables
one to make fairly accurate prediction of properties of the polymer.
✓The relevant factors to be considered are:
Relation of Structure and properties of polycarbonate
Polycarbonate structure
(a) The presence of benzene rings in the chain restricts flexibility of the molecule.
(b) The repeating unit of the molecule is quite long.
Physical Properties
Acids—concentrated Poor
Acids—dilute Good
Alcohols Good
Alkalis Good
Aromatic hydrocarbons Poor
oils Good
Halogenated hydrocarbons Good
Halogens Poor
Ketones Poor
Chemical Resistance
POLYCARBONATE
MANUFACTURING
Introduction
❑Polycarbonate has two main types; bis-phenol A polycarbonate and non
bis-phenol A polycarbonate which has 7types.
❑ Bis-phenol A polycarbonate is manufactured using two methods of
polymerization, because the second monomer that added to bisphenol A
so if phosgene is added the polymerization method used is interfacial
polymerization and which the commercially method for production
polycarbonate, the other polymerization method done by using do-
phenyl carbonate instead of phosgene which known as melt
polymerization, the main advantage in this method is safety of di-phenyl
carbonate with opposite that toxicity of phosgene.
Process description
Stages of production
❑Production of polycarbonate pass through three stages; starting from reaction
of bis-phenol A and phosgene, then separation process until getting
polycarbonate powder and finally extrusion and drying PC-pellets and
packaging it.
❑In production of polycarbonate by interfacial polymerization method these
raw materials are required;
1- Solution of Bis-Phenol A and methylene chloride.
2- Phosgene in liquid form at 8.2°C.
3- Phenol in liquid form at 4°C, which used as molecular weight regulator, to
inactivate some
carbonate oligomer ends to get required weight.
4- Triethylamine added in liquid form at 20°C used as catalyst to prevent revere
of reaction.
5- Sodium hydroxide is added in solid form to get sodium salt of bis-phenol A.
(1) Reaction
The interfacial polymerization done
in patch reactor on two process;
❑ first bis-phenol A reacts with
sodium hydroxide to get sodium
salt of bis-phenol A at 25-30°C in
average time 25 minute as shown
in equation (1).
❑ after that and at same
temperature phosgene react with
sodium salt of bisphenol A to get
polycarbonate as shown in
equation (2).
(2) Separation
The target of separation process is releasing polycarbonate powder from chemicals of
previous stage and this occur in two stages using two units; centrifuge and
concentrator.
A- Centrifuge
It used for extraction catalyst and impurities such as; NaCl, and phenol from poly
carbonate solution, for ensuring that there’s no rest of catalyst and impurities 4
centrifuge are used for this process.
The desalinated water is used to wash product of reaction with rotational speed 2 rpm
for separating impurities from PC-solution.
B- Concentrator
After centrifuges polycarbonate and methylene chloride solution pass through a
concentrator at which an anti-solvent such as methanol added in liquid form for
precipitations process for separating Polycarbonate powder from methylene chloride.
(3) Extrusion & Pelletizing& Drying & Packaging
A- Extrusion
❑ After precipitation process poly carbonate powder passed through
an extruder, it may be single or twin-screw extruder, and since
extruder work with direct extrusion technique talk powder addedto
reduce friction, poly carbonate melted at 250°C so through group
of parallel heaters.
❑ The extruder used is German-made Werner which is twin screw
extruder which are capable of rotating between 146 rpm and 172
rpm the extruder has eleven zone polymer powder passes through
it to be in molten shape until it reaches to head of extruder (die), a
solid steel plate with 986 holes in it to form the molten powder into
ribbons
B- Pelletizing
After extruding molten ribbons pass through tank of water supplied
with water pump to cool these ribbons, after that cooled ribbons cut
with blades set at axis it may be 16, 20, 24 knifes, the pelletizer
rotates with 600 to 850 rpm.
C- Drying
For getting red of moisture poly carbonate pellets dried using a dryer
unit at 120°C, this process takes between 3 to 4 hours to be sure that
the pellets dried well.
D- Packaging
Finally, after drying process polymer pellets pass through streams
and by using open gate valve it put in silos to be packaged.
POLYCARBONATE
APPLICATIONS
❑Electricals and Electronics
❑Construction materials
❑Medical application
❑Automotive
❑Face Shields
❑Polycarbonate blends
Polycarbonate is blended with other polymers to enhance its properties
such as ABS, PBT, PET;
o PC/ABS (Acrylonitrile Butadiene Styrene)
In a compounded blend of polycarbonate and ABS, as he
polycarbonate contributions impact and heat resistance,
while the ABS contributions chemical stress resistance, and
cost reduction below polycarbonate
Uses
▪ Flash light
▪ Phones
▪ Safety helmets
▪ Laptop case
POLYCARBONATE
HANDLING & STORAGE
Polycarbonate Handling
❑Toxicity
✓ Polycarbonate is non-toxic as it manufactured mainly from Bis-phenolA which is
free of test and smell.
✓ just in case of manufacturing it using phosgination method the used phosgene is
toxic but after manufacturing process done there is no dangerous
❑Flammability
✓Incase of there’s ignition source, polycarbonate burns with sooty flame.
✓It extinguishes after ignition source is removed.
✓carbon di-oxide, carbon monoxide, phenol are very dangerous products if combustion
process occur so, the following safety tools must be put in consideration;
1-Skin: Fabric gloves are recommended when handling molten material.
2-Eye: Safety glasses are recommended for eye protection.
3-For fire fighting: full emergency equipment with self-contained breathing apparatus be
worn by fire fighters
Polycarbonate storage
Polycarbonate storing at SABIC company stores
POLYCARBONATE
MANUFACTURERS
oSabic.
oEPC Group.
oDOW.
oBayar.
THANKS FOR ATTENTION
Any Questions???

Polycarbonate

  • 1.
    Higher Technological Institute-10thof Ramadan City Department of Chemical Engineering 2018 Presented by Students AbdAl-Rhman Magdy AbdullahYoussef 20160517 AbdAl-Rhman Ali Basheer 20160476 Amr Ahmed Saeed 20160629 Supervisors Prof. Maher Gamal Professor of Chemical Engineering Department of Chemical Engineering HigherTechnological Institute-10th of Ramadan City Eng. MohammedYahiya AssistantTeacher Department of Chemical Engineering HigherTechnological Institute-10th of Ramadan City POLYCARBONATE November
  • 2.
  • 3.
    Introduction ✓ Polycarbonate orLexan was discovered by; Dr. Hermann Schell and his team at Bayar company in 1953. ✓ It is a condensation product of bisphenol A, and a carbonate donner such as phosgene or diphenyl carbonate. ✓ Industrially it manufactured by; ❑ Interfacial polymerization (Bisphenol-A+Phosgene). ✓ It can be processed by Extrusion or Injection molding. ✓ Polycarbonate is a good engineering thermoplastic material having many good optical, thermal, electrical and mechanical properties. ✓ It has many applications in different fields such as; electronics and automotive. ❑ Melt polymerization (Bisphenol-A+Di-Phenyl carbonate)
  • 4.
  • 5.
    ✓ A studyof the molecular structure of bis-phenol A polycarbonates enables one to make fairly accurate prediction of properties of the polymer. ✓The relevant factors to be considered are: Relation of Structure and properties of polycarbonate Polycarbonate structure (a) The presence of benzene rings in the chain restricts flexibility of the molecule. (b) The repeating unit of the molecule is quite long.
  • 6.
  • 7.
    Acids—concentrated Poor Acids—dilute Good AlcoholsGood Alkalis Good Aromatic hydrocarbons Poor oils Good Halogenated hydrocarbons Good Halogens Poor Ketones Poor Chemical Resistance
  • 8.
  • 10.
    Introduction ❑Polycarbonate has twomain types; bis-phenol A polycarbonate and non bis-phenol A polycarbonate which has 7types. ❑ Bis-phenol A polycarbonate is manufactured using two methods of polymerization, because the second monomer that added to bisphenol A so if phosgene is added the polymerization method used is interfacial polymerization and which the commercially method for production polycarbonate, the other polymerization method done by using do- phenyl carbonate instead of phosgene which known as melt polymerization, the main advantage in this method is safety of di-phenyl carbonate with opposite that toxicity of phosgene. Process description
  • 11.
    Stages of production ❑Productionof polycarbonate pass through three stages; starting from reaction of bis-phenol A and phosgene, then separation process until getting polycarbonate powder and finally extrusion and drying PC-pellets and packaging it. ❑In production of polycarbonate by interfacial polymerization method these raw materials are required; 1- Solution of Bis-Phenol A and methylene chloride. 2- Phosgene in liquid form at 8.2°C. 3- Phenol in liquid form at 4°C, which used as molecular weight regulator, to inactivate some carbonate oligomer ends to get required weight. 4- Triethylamine added in liquid form at 20°C used as catalyst to prevent revere of reaction. 5- Sodium hydroxide is added in solid form to get sodium salt of bis-phenol A.
  • 12.
    (1) Reaction The interfacialpolymerization done in patch reactor on two process; ❑ first bis-phenol A reacts with sodium hydroxide to get sodium salt of bis-phenol A at 25-30°C in average time 25 minute as shown in equation (1). ❑ after that and at same temperature phosgene react with sodium salt of bisphenol A to get polycarbonate as shown in equation (2).
  • 13.
    (2) Separation The targetof separation process is releasing polycarbonate powder from chemicals of previous stage and this occur in two stages using two units; centrifuge and concentrator. A- Centrifuge It used for extraction catalyst and impurities such as; NaCl, and phenol from poly carbonate solution, for ensuring that there’s no rest of catalyst and impurities 4 centrifuge are used for this process. The desalinated water is used to wash product of reaction with rotational speed 2 rpm for separating impurities from PC-solution. B- Concentrator After centrifuges polycarbonate and methylene chloride solution pass through a concentrator at which an anti-solvent such as methanol added in liquid form for precipitations process for separating Polycarbonate powder from methylene chloride.
  • 14.
    (3) Extrusion &Pelletizing& Drying & Packaging A- Extrusion ❑ After precipitation process poly carbonate powder passed through an extruder, it may be single or twin-screw extruder, and since extruder work with direct extrusion technique talk powder addedto reduce friction, poly carbonate melted at 250°C so through group of parallel heaters. ❑ The extruder used is German-made Werner which is twin screw extruder which are capable of rotating between 146 rpm and 172 rpm the extruder has eleven zone polymer powder passes through it to be in molten shape until it reaches to head of extruder (die), a solid steel plate with 986 holes in it to form the molten powder into ribbons
  • 15.
    B- Pelletizing After extrudingmolten ribbons pass through tank of water supplied with water pump to cool these ribbons, after that cooled ribbons cut with blades set at axis it may be 16, 20, 24 knifes, the pelletizer rotates with 600 to 850 rpm. C- Drying For getting red of moisture poly carbonate pellets dried using a dryer unit at 120°C, this process takes between 3 to 4 hours to be sure that the pellets dried well. D- Packaging Finally, after drying process polymer pellets pass through streams and by using open gate valve it put in silos to be packaged.
  • 16.
  • 17.
    ❑Electricals and Electronics ❑Constructionmaterials ❑Medical application ❑Automotive ❑Face Shields
  • 18.
    ❑Polycarbonate blends Polycarbonate isblended with other polymers to enhance its properties such as ABS, PBT, PET; o PC/ABS (Acrylonitrile Butadiene Styrene) In a compounded blend of polycarbonate and ABS, as he polycarbonate contributions impact and heat resistance, while the ABS contributions chemical stress resistance, and cost reduction below polycarbonate Uses ▪ Flash light ▪ Phones ▪ Safety helmets ▪ Laptop case
  • 19.
  • 20.
    Polycarbonate Handling ❑Toxicity ✓ Polycarbonateis non-toxic as it manufactured mainly from Bis-phenolA which is free of test and smell. ✓ just in case of manufacturing it using phosgination method the used phosgene is toxic but after manufacturing process done there is no dangerous ❑Flammability ✓Incase of there’s ignition source, polycarbonate burns with sooty flame. ✓It extinguishes after ignition source is removed. ✓carbon di-oxide, carbon monoxide, phenol are very dangerous products if combustion process occur so, the following safety tools must be put in consideration; 1-Skin: Fabric gloves are recommended when handling molten material. 2-Eye: Safety glasses are recommended for eye protection. 3-For fire fighting: full emergency equipment with self-contained breathing apparatus be worn by fire fighters
  • 21.
  • 22.
  • 23.
  • 24.