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General Approaches to Polymer Synthesis

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Presentation on theme: "General Approaches to Polymer Synthesis"— Presentation transcript:

1 General Approaches to Polymer Synthesis
1. Addition Chain Growth Polymerization of Vinyl Monomers Ring Opening Polymerization Heterocylics Metathesis of Cyclic Olefins 2. Condensation Step Growth   Polymerization of A-B or AA/BB Monomers 3. Modification of Preformed Polymers Polysaccharides Peptides and Proteins   Synthetic Precursors

2 Current Strategies in Polymer Synthesis
Objectives: Precise Macromolecular Design 1 . Control of: Molecular Weight Molecular Weight Distribution Composition Sequence of repeat units Stereochemistry 2.  Versatility

3 Free Radical Initiated Polymerization
Classical Free Radical Process Applied to wide range of monomers Broad scope of experimental conditions Molecular weight can be controlled Mw/Mn > 1.5  2.0  Statistical compositions and sequences Little stereochemical control

4 Anatomy of Addition Polymerizations
Initiation Generation of active initiator Reaction with monomer to form growing chains Propagation Chain extension by incremental monomer addition Termination Conversion of active growing chains to inert polymer Chain Transfer Transfer of active growing site by terminating one chain and reinitiating a new chain.

5 Polymerizability of Vinyl Monomers
Active Centers must be stable enough to persist though multiple monomer additions Typical vinyl monomers

6 Polymerizability of Vinyl Monomers
Radical Cationic Anionic Complex Metal Ethylene + - Propylene +/- 1,1-Dialkyl olefins 1,2-Dialkyl olefins 1,3-Dienes Styrenes

7 Polymerizability of Vinyl Monomers
Radical Cationic Anionic Complex Metal VCl + - +/- Vinyl esters Acylates/ methacrylates Acrylonitriles/ Acrylamides Vinyl ethers Substituted Styrenes

8 Types of Vinyl Polymerization
Method Advantages Disadvantages Bulk (Neat) Simple equipment Rapid reaction Pure polymer isolated Heat buildup Gel effect Branched or crosslinked product Solution Good mixing Ready for application Lower mol. Wt. Low Rpoly Solvent Recovery Suspension (Pearl) Low viscosity Direct bead formation Removal of additives Emulsion High Rpoly Low Temperatures High Mol. Wt. High surface area latex Coagulation needed Latex stability Inverse Emulsion Water in oil latex formed Inversion promotes dissolution in water

9 Thermodynamics of Polymerization

10 Thermodynamics of Polymerization
Monomer -DHp, kJ/mole -DSp, J/K-mole Tc, K (C) Observed Ethylene 93 155 600 (327) 400 MMA 56 104 478(205) 220 a-Methyl styrene 35 110 318 (45) 61 Isobutylene 48 121 326 ( 123) 50

11 Suspension Polymerization
Equivalent to a "mini-bulk" polymerization Advantages Aqueous (hydrocarbon) media provides good heat transfer Good particle size control through agitation and dispersion agents Control of porosity with proper additives and process conditions Product easy to recover and transfer Disadvantages Suspending Agents contaminate product Removal of residual monomer necessary

12 Suspension (Pearl) Polymerization
Process Type Aqueous Phase Monomers Used Product BEAD Polymer Soluble in Monomer  1% Sol. Polymer Suspending Agents Cu++ Inhibitors Styrene Methyl Methacrylate Vinyl Acetate Clear Beads POWDER Polmer Insoluble in Monomer Suspending Agents Electrolytes Vinyl Chloride Acrylonitrile Fluoroethylene Opaque Beads or Powders INVERSE Hydrocarbon Media Monomer Initiator Acrylamide Acrylic Acids Beads  Emulsions

13 Suspension Polymerization of Styrene
Monomer Phase 16.6 Kg. Styrene (0.5 kg Methacrylic Acid) 0.012 kg AIBN 0.006 kg Benzoyl Peroxide 0.015 kg tert-Butyl Perbenzoate Temp Aqueous Phase: Kg of H2O 0.24 kg Ca3PO4 0.14 kg Na+ Naphthalene sulfonate 0.077 kg. 15% Sodium Polyacrylate Polymerization Time. Hours

14 EMULSION POLYMERIZATION
Advantages: High rate of polymerization High molecular weights Few side reactions High Conversion achieved Efficient heat transfer Low viscosity medium Polymer never in solution Low tendancy to agglomerate Emulsified polymer may be stabilized and used directly Disadvantages: Polymer surface contaminated by surface active agents Coagulation introduces salts;Poor electrical properties

15 Components of Emulsion Polymerization
Water soluble initiator

16 POLYMERS PRODUCED USING EMULSION PROCESSES
Applications Styrene-Butadiene Rubber (SBR) Tires, Belting, Flooring, Molded goods, Shoe soles, Electrical insulation Butadiene-Acrylonitrile (nitrile rubber) Fuel tanks, Gasoline hoses, Adhesives, Impregnated paper, leather and textiles Acrylonitrile-Butadiene-Styrene (ABS) Engineering plastics, household appliances, Automobile parts, Luggage Polyacrylates Water based latex paints

17 Major Developments in the 1950-60's
Living Polymerization (Anionic) Mw/Mn  1 Blocks, telechelics and stars available (Controlled molecular architecture) Statistical Stereochemical Control Statistical Compositions and Sequences Severe functional group restrictions

18 Ziegler-Natta (Metal-Coordinated) Polymerization
Stereochemical Control Polydisperse products Statistical Compositions and Sequences Limited set of useful monomers, i.e. olefins SINGLE SITE CATALYSTS

19 Polyolefins Polypropylene (1954) PP
dishwasher safe plastic ware, carpet yarn, fibers and ropes, webbing, auto parts

20 Tacticity Isotactic Syndiotactic Heterotactic (Atactic)
All asymmetric carbons have same configuration Methylene hydrogens are meso Polymer forms helix to minimize substituent interaction Syndiotactic Asymmetric carbons have alternate configuration Methylene hydrogens are racemic Polymer stays in planar zig-zag conformation Heterotactic (Atactic) Asymmetric carbons have statistical variation of configuration

21 Additional Developments in the 1980's
"Immortal" Polymerization (Cationic) Mw/Mn  1.05 Blocks, telechelics, stars (Controlled molecular architecture) Statistical Compositions and Sequences Severe functional group restrictions

22 Free Radical Initiated Polymerization
Controlled Free Radical Polymerization Broad range of monomers available Accurate control of molecular weight Mw/Mn  Almost monodisperse Blocks, telechelics, stars (Controlled molecular architecture) Statistical Compositions and Sequences

23 Genetic Approaches via Modified Microorganisms
Monodisperse in MW Monodisperse in Composition Sequentially Uniform Stereochemically Pure Diverse set of functional groups possible through synthesis of novel amino acids

24 Commodity Polyolefins
Polyethylene High Density (1954) HDPE Bottles, drums, pipe, conduit, sheet, film Low Density ( ) LDPE Packaging Film, wire and cable coating, toys, flexible bottles, house wares, coatings Linear Low Density (1975) Shirt bags, high strength films LLDE

25 Commodity Polyolefins
Polypropylene (1954) PP dishwasher safe plastic ware, carpet yarn, fibers and ropes, webbing, auto parts Polyisobutylene (1940) PIB inner tubes, flexible adhesives, raincoats

26 Commodity Vinyl Polymers
Polystyrene (1920) PS Styrofoam, clear plastic cups envelop windows, toys Poly(vinyl chloride) (1927) PVC garden hose, pipe, car trim, seat covers, records, floor tiles

27 Semi-Commodity Polymers
Poly(methyl methacrylate) (1931) PMMA plexiglas, embedding resin, resist for X-ray applications Polytetrafluoroethylene. (1943) teflon, non stick cookware, no grease bearings, pipe-seal tape

28 Commodity Condensation Polymers
Nylon 6 / bearings, molded parts carpet yarn marine rope cooking/boiling bags Nylon 66 (1939) Fibers, tire cord, fishing line

29 Commodity Condensation Polymers
Polyester (1941) PET, dacron, mylar, kodel fibers, film-backing, magnetic tapes, soft drink bottles, tire cord, moldings Polycarbonate (1957) PC, Lexan shatter proof glass, cd-disks, car doors and roofs, appliance housings


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