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PVC

n= 625 to 2700 (Mw = 39000-168000 g/mol)

October 30, 2013

PVC

1
Year 2000

October 30, 2013

PVC

2
Bahan Mentah
2CH 4 → C 2 H 2 + 3H 2

H 2 C = CH 2 + Cl 2 → ClH 2 C − CH 2 Cl → HCl + H 2 C = CHCl

October 30, 2013

PVC

3
Kandungan Klorin

October 30, 2013

PVC

4
Vinyl & Fire
☺Kandungan ~ 50 % klorin

⇒ Hanya menyediakan setengah
bahan bakar daripada polimer lainnya

☺Perangkap radikal, peracunan mekanisme api
R− X

+

Flame
retardant

H ~~~~~~~

→ R•

Bahan Bakar
Hidrogen

+

Flame retardant
fragment

H − Cl

+

• ~~~~~~~~
Bahan Bakar,
kekurangan
hidrogen

☺ Karbon monoksida

October 30, 2013

PVC

5
Polimerisasi
 Polimerisasi
radikal bebas

October 30, 2013

PVC

6
Polimerisasi
VCM vs. Oksigen
O2 tidak diinginkan
O2 ⇒ R-O-O-R' +VCM
⇒ poli (vinil klorid
peroksida
O2 dideteksi , Kenapa?

October 30, 2013

VCM vs. Nitrogen
N2 larut dalam VCM
(Jadi, apa??)
1. Pengangkutan monomer
2. Menekan pembangunan

Bagaimana bisa kita bergerak monomer???

Monomer digerakan oleh:
 Pompa
 Pemanasan
 Grafitasi

PVC

7
Polimerisasi
Suspensi polimerisasi banyak digunakan,
karena :
1. Titik didih monomer yang rendah.
(Stabilitas PVC)
2. PVC saling larut dengan monomer nya.

October 30, 2013

PVC

8
PVC solubility in its monomer
PVC tidak larut dalam monomernya sendiri. PVC
sebagai endapan partikel kecil selama polimerisasi.
Ini aglomerat yang struktur internal berpori.

VCM ini cukup larut dalam PVC:
 PVC melunak dengan monomer.
 Tingkat polimerisasi VCM dalam partikel yang
bengkak secara substansial lebih cepat dari laju
polimerisasi dalam fase cair (Mengapa?)

October 30, 2013

PVC

9
Kelarutan PVC dalam monomernya
Percepatan Auto
Seiring dengan peningkatan konversi  polimer Lebih
terbentuk  monomer Lebih mengalami
pembengkakan didalam polimer
For long half-life initiator, R ∝ Conversion
p

However, long half-life initiators are not used, so
reaction acceleration tends to drop off as the active
initiator is consumed.

October 30, 2013

PVC

10
Polimerisasi kinetika

Eksotermik: panas yang dihasilkan oleh reaksi
Panas total beban: panas aktual harus
dihilangkan

October 30, 2013

PVC

11
berat molekul
Mw of PVC is controlled by altering the
polymerization temperature, chain transfer to
monomer controls the Mw.
T ↑ Mw↓ (why?)
Karena kenaikan suhu, meningkatkan laju perpindahan
rantai lebih cepat daripada tingkat perambatan rantai.

October 30, 2013

PVC

12
MWD
Isothermal ⇒ Narrow MWD
Temperature ramped ⇒ Broad MWD
T

t
October 30, 2013

PVC

13
Polimerisasi Suhu Reaksi
Suhu Polimerisasi 50 ° C – 70 ° C
T < 50 ° C:
Tingkat Polimerisasi terlalu lambat dan MW
terlalu tinggi.
T > 70 ° C: P terlalu tinggi

October 30, 2013

PVC

14
Pemindah rantai untuk monomer

October 30, 2013

PVC

15
Perpanjangan berat molekul
To produce high-Mw PVC, there are two options:

1.
2.

Lower temperature (T<50° C) BUT…
Add multifunctional monomer as di-allyl
phthalate, Be careful…

October 30, 2013

PVC

16
Perpanjangan Berat Molekul
More challenging task…
To produce low-Mw PVC, there are two options:
1. Reduce temperature, BUT…
2. Use chain-transfer agent

October 30, 2013

PVC

17
Struktur
PVC memiliki struktur linier
Head to tail is most common

PVC shows a tendency to add via syndiotactic
placement ⇒ low crystallinity
October 30, 2013

PVC

18
PVC facts

Other 5%

Annual demand close to 30 Mton

Transport 7%

Annual growth of 4%
Electronics 8%

75% by suspension polymerization
Consumer
goods 10%

Wide variety of applications

Building 60%

October 30, 2013

PVC

Packaging 10%

19
Stability
PVC is the least stable polymer in commercial use.
PVC degrades as it is exposed to high temperatures, high
mechanical stress or ultraviolet (UV) light.
This may take place during processing, storage and
utilization.
Degradation causes discoloration, deterioration of
mechanical properties and lowering of chemical resistance.
Degradation of polymer occurs by successive elimination of
HCl (dehydrochlorination) yielding polyenes.

October 30, 2013

PVC

20
Stabilitas

October 30, 2013

PVC

21
Stabilitas
Stabilization mainly proceeds by the addition of
compounds as: metal oxides, carbonates, fatty acid
salts as well as HCl acceptors as ethylene oxide
compounds.
These additives stabilize PVC by:
1. slowing down the dehydroclorination reaction.
2. absorption of the evolved HCl.

October 30, 2013

PVC

22
Thermal stability

Polymer microstructure

tertiary chlorine

Chain branches
Structural defects

• Long chain branches
(R > 4 C atoms)

• Short chain branches
(R ≤ 4 C atoms)

C l

C l R

C l

Internal double bonds
allylic chlorine
October 30, 2013

PVC

23
Stabilitas
 Thermal stability decreases when monomer conversion
increases (WHY?)

October 30, 2013

PVC

24
Plasticization
It is defined as converting PVC, which is a rigid
polymer, to flexible PVC.
Plasticization improves flexibility by acting as an
internal lubricant between PVC chains.
 For a plasticizer to be effective, it must be
thoroughly mixed and incorporated into the PVC
polymer matrix.

October 30, 2013

PVC

25
Plasticization
 Plasticization theories:
Lubricating theory: as the system is heated, the
plasticizer molecules diffuse into the polymer and
weaken the polymer-polymer interactions (van der
Waals' forces). According to this theory the
plasticizer molecules act as shields to reduce
polymer-polymer interactive forces and prevent the
formation of a rigid network.

October 30, 2013

PVC

26
Plasticization
 Plasticization theories:
Gel theory: considers the plasticized polymer to be
neither solid nor liquid but an intermediate state,
loosely held together by a three-dimensional
network of weak secondary bonding forces. These
bonding forces acting between plasticizer and
polymer are easily overcome by applied external
stresses allowing the plasticized polymer to flex,
elongate, or compress.

October 30, 2013

PVC

27
Copolymers
¤ VCM does not copolymerize well. It has an unfavorable reactivity
ratio with just about every other monomer except vinyl acetate
(VAC).

¤ Because of the unfavorable reactivity ratios, making other
copolymers usually involves long reactions with slow metering of
one of the monomers (the one that reacts fastest).
¤ PVC is insoluble in the monomer and this produces the porous
internal structure. One of the reasons for this insolubility is that
the polymer has a certain level of crystallinity ⇒ This produces a
non-porous particle.

October 30, 2013

PVC

28
Copolymers
¤ most copolymers are made using microsuspension or emulsion
methods , because these processes produce small particles that can
be stripped of residual monomer.
¤ Copolymers entangle and fuse at lower temperatures and flow
more easily at lower melt temperatures, because they have low or
no crystallinity.

October 30, 2013

PVC

29

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PVC

  • 1. PVC n= 625 to 2700 (Mw = 39000-168000 g/mol) October 30, 2013 PVC 1
  • 3. Bahan Mentah 2CH 4 → C 2 H 2 + 3H 2 H 2 C = CH 2 + Cl 2 → ClH 2 C − CH 2 Cl → HCl + H 2 C = CHCl October 30, 2013 PVC 3
  • 5. Vinyl & Fire ☺Kandungan ~ 50 % klorin ⇒ Hanya menyediakan setengah bahan bakar daripada polimer lainnya ☺Perangkap radikal, peracunan mekanisme api R− X + Flame retardant H ~~~~~~~ → R• Bahan Bakar Hidrogen + Flame retardant fragment H − Cl + • ~~~~~~~~ Bahan Bakar, kekurangan hidrogen ☺ Karbon monoksida October 30, 2013 PVC 5
  • 7. Polimerisasi VCM vs. Oksigen O2 tidak diinginkan O2 ⇒ R-O-O-R' +VCM ⇒ poli (vinil klorid peroksida O2 dideteksi , Kenapa? October 30, 2013 VCM vs. Nitrogen N2 larut dalam VCM (Jadi, apa??) 1. Pengangkutan monomer 2. Menekan pembangunan Bagaimana bisa kita bergerak monomer??? Monomer digerakan oleh:  Pompa  Pemanasan  Grafitasi PVC 7
  • 8. Polimerisasi Suspensi polimerisasi banyak digunakan, karena : 1. Titik didih monomer yang rendah. (Stabilitas PVC) 2. PVC saling larut dengan monomer nya. October 30, 2013 PVC 8
  • 9. PVC solubility in its monomer PVC tidak larut dalam monomernya sendiri. PVC sebagai endapan partikel kecil selama polimerisasi. Ini aglomerat yang struktur internal berpori. VCM ini cukup larut dalam PVC:  PVC melunak dengan monomer.  Tingkat polimerisasi VCM dalam partikel yang bengkak secara substansial lebih cepat dari laju polimerisasi dalam fase cair (Mengapa?) October 30, 2013 PVC 9
  • 10. Kelarutan PVC dalam monomernya Percepatan Auto Seiring dengan peningkatan konversi  polimer Lebih terbentuk  monomer Lebih mengalami pembengkakan didalam polimer For long half-life initiator, R ∝ Conversion p However, long half-life initiators are not used, so reaction acceleration tends to drop off as the active initiator is consumed. October 30, 2013 PVC 10
  • 11. Polimerisasi kinetika Eksotermik: panas yang dihasilkan oleh reaksi Panas total beban: panas aktual harus dihilangkan October 30, 2013 PVC 11
  • 12. berat molekul Mw of PVC is controlled by altering the polymerization temperature, chain transfer to monomer controls the Mw. T ↑ Mw↓ (why?) Karena kenaikan suhu, meningkatkan laju perpindahan rantai lebih cepat daripada tingkat perambatan rantai. October 30, 2013 PVC 12
  • 13. MWD Isothermal ⇒ Narrow MWD Temperature ramped ⇒ Broad MWD T t October 30, 2013 PVC 13
  • 14. Polimerisasi Suhu Reaksi Suhu Polimerisasi 50 ° C – 70 ° C T < 50 ° C: Tingkat Polimerisasi terlalu lambat dan MW terlalu tinggi. T > 70 ° C: P terlalu tinggi October 30, 2013 PVC 14
  • 15. Pemindah rantai untuk monomer October 30, 2013 PVC 15
  • 16. Perpanjangan berat molekul To produce high-Mw PVC, there are two options: 1. 2. Lower temperature (T<50° C) BUT… Add multifunctional monomer as di-allyl phthalate, Be careful… October 30, 2013 PVC 16
  • 17. Perpanjangan Berat Molekul More challenging task… To produce low-Mw PVC, there are two options: 1. Reduce temperature, BUT… 2. Use chain-transfer agent October 30, 2013 PVC 17
  • 18. Struktur PVC memiliki struktur linier Head to tail is most common PVC shows a tendency to add via syndiotactic placement ⇒ low crystallinity October 30, 2013 PVC 18
  • 19. PVC facts Other 5% Annual demand close to 30 Mton Transport 7% Annual growth of 4% Electronics 8% 75% by suspension polymerization Consumer goods 10% Wide variety of applications Building 60% October 30, 2013 PVC Packaging 10% 19
  • 20. Stability PVC is the least stable polymer in commercial use. PVC degrades as it is exposed to high temperatures, high mechanical stress or ultraviolet (UV) light. This may take place during processing, storage and utilization. Degradation causes discoloration, deterioration of mechanical properties and lowering of chemical resistance. Degradation of polymer occurs by successive elimination of HCl (dehydrochlorination) yielding polyenes. October 30, 2013 PVC 20
  • 22. Stabilitas Stabilization mainly proceeds by the addition of compounds as: metal oxides, carbonates, fatty acid salts as well as HCl acceptors as ethylene oxide compounds. These additives stabilize PVC by: 1. slowing down the dehydroclorination reaction. 2. absorption of the evolved HCl. October 30, 2013 PVC 22
  • 23. Thermal stability Polymer microstructure tertiary chlorine Chain branches Structural defects • Long chain branches (R > 4 C atoms) • Short chain branches (R ≤ 4 C atoms) C l C l R C l Internal double bonds allylic chlorine October 30, 2013 PVC 23
  • 24. Stabilitas  Thermal stability decreases when monomer conversion increases (WHY?) October 30, 2013 PVC 24
  • 25. Plasticization It is defined as converting PVC, which is a rigid polymer, to flexible PVC. Plasticization improves flexibility by acting as an internal lubricant between PVC chains.  For a plasticizer to be effective, it must be thoroughly mixed and incorporated into the PVC polymer matrix. October 30, 2013 PVC 25
  • 26. Plasticization  Plasticization theories: Lubricating theory: as the system is heated, the plasticizer molecules diffuse into the polymer and weaken the polymer-polymer interactions (van der Waals' forces). According to this theory the plasticizer molecules act as shields to reduce polymer-polymer interactive forces and prevent the formation of a rigid network. October 30, 2013 PVC 26
  • 27. Plasticization  Plasticization theories: Gel theory: considers the plasticized polymer to be neither solid nor liquid but an intermediate state, loosely held together by a three-dimensional network of weak secondary bonding forces. These bonding forces acting between plasticizer and polymer are easily overcome by applied external stresses allowing the plasticized polymer to flex, elongate, or compress. October 30, 2013 PVC 27
  • 28. Copolymers ¤ VCM does not copolymerize well. It has an unfavorable reactivity ratio with just about every other monomer except vinyl acetate (VAC). ¤ Because of the unfavorable reactivity ratios, making other copolymers usually involves long reactions with slow metering of one of the monomers (the one that reacts fastest). ¤ PVC is insoluble in the monomer and this produces the porous internal structure. One of the reasons for this insolubility is that the polymer has a certain level of crystallinity ⇒ This produces a non-porous particle. October 30, 2013 PVC 28
  • 29. Copolymers ¤ most copolymers are made using microsuspension or emulsion methods , because these processes produce small particles that can be stripped of residual monomer. ¤ Copolymers entangle and fuse at lower temperatures and flow more easily at lower melt temperatures, because they have low or no crystallinity. October 30, 2013 PVC 29

Notes de l'éditeur

  1. PVC was first produced commercially in the late 1920s and is now one of the most widely used plastics. PVC is used in :-medical applications (due to its safety, chemical stability and compatibility) -transport (floor modules of cars etc., good because of its low energy consumption) -building and construction (50% of western consumption, mostly piping, flooring and profiles)-light, easy to install, fire resistant) -consumer goods and daily life -packaging It was not until the late 1920s that the first commercial production of PVC took place in the USA.  PVC was first used instead of rubber to insulate the wires in electrical cables during Word War II, when rubber was in short supply. Since then it has replaced rubber for insulation and found many other applications. Today PVC is the second most popular plastic in the world. 30% of total thermoplastic manufacturing