Polymerization reactions chapter 4. Fall 20111. outline Introduction Classifications Chain...
-
Upload
eric-cummings -
Category
Documents
-
view
231 -
download
2
Transcript of Polymerization reactions chapter 4. Fall 20111. outline Introduction Classifications Chain...
chapter 4. Fall 2011 1
Polymerization reactions
chapter 4. Fall 2011 2
outline
• Introduction• Classifications• Chain Polymerization (free radical initiation)• Reaction Mechanism• Kinetic Rate Expressions• Definition of a Rate Equation• Rate Expressions for Styrene Polymerization• QSSA (Quasi-steady state assumption)
chapter 4. Fall 2011 3
• we start an engineering discussion of polymers by addressing how they are made
• beyond the selection of the monomer building blocks, the polymerization process is most important to properties: it sets the configuration
• you should be able to model polymerizations and determine the effects of changing monomers, temperature, pressure and other variables
chapter 4. Fall 2011 4
classifications
Chain Polymerization (example: polystyrene)• monomer is added to the active center• high polymer is made in small quantities
continuously• monomer concentration is decreased
slowly• high molecular weight polymers are made
when the concentration of active centers is low
chapter 4. Fall 2011 5
• Step Polymerization (example: nylon 6,6)• · end groups of the monomers react• · monomer is depleted rapidly• · high molecular weight polymer is made
slowly•
chapter 4. Fall 2011 6
Chain vs. stepChain Step
Only species with active centers add monomer units
Any two potentially reactive end groups can react
Monomer concentration decreases steadily
Monomer depletion occurs very rapidly
High molecular weight polymer forms at once
Polymer molecular weight increases slowly with time
The concentration of reacting chains is usually low compared to the non-reacting monomer and polymer
Any size species can react with another, and many chains are reacting at one time
chapter 4. Fall 2011 7
Typical vinyl monomersNo homopolymerization Typical
homopolymerizationRapid homopolymerization
A- methyl styrene ethylene Hydroxy methyl vinyl ketone
Allyl alcohol propylene Vinylidene cyanide
stilbene isobutylene Acrylic acid
dichloroethylene butadiene Acrylic anhydride
Maleic acid Vinyl chloride Methylene malonate
Vinyl esters, ethers nitroethylene
See Table 4.3 on methods of manufacturing for vinyl polymers
chapter 4. Fall 2011 8
chapter 4. Fall 2011 9
Chain polymerization(free radical initiation)
· monomers have double bonds· typical monomers shown in Table 4.2· bulk: only monomer present· emulsion: latex particles < 1 micron· suspension: particles between 50 to 500 microns· solution: monomer is dissolved in a second liquid· particle morphology has commercial value
chapter 4. Fall 2011 10
Reaction mechanism
• We will learn a generic reaction mechanism which can
be modified to describe many chain polymerization. Each step can be described by a reaction rate expression. The overall reaction rate model gives us the change in the monomer concentration with time, which can be used for process control.
• • • .
chapter 4. Fall 2011 11
Initiation (formation of free radicals)
[initiators, catalysts] Benzoyl peroxide
The radical can react with a double bond, linking the initiator fragment with the monomer. The reactive site moves to the end of the chain
chapter 4. Fall 2011 12
Propagation
The active center adds monomer, transfer the radical to the new unit, and continues.
chapter 4. Fall 2011 13
Termination
C* C*+
polymer
chapter 4. Fall 2011 14
Reaction Kinetics• The minimum set of reactions which describe a free radical
polymerization are:• • initiation,• propagation, and• termination.• • More complex systems could include:• multiple initiation, propagation, or termination steps;• side reactions such as:
– chain branching,– monomer or polymer degradation, – chain transfer, etc.
chapter 4. Fall 2011 15
We will write general equations for simple systems, and you should be able to add as much complexity as you want for a specific system.
chapter 4. Fall 2011 16
chapter 4. Fall 2011 17
chapter 4. Fall 2011 18
chapter 4. Fall 2011 19
We have generated four rate equations which describe a simple polymerization. The one which relates directly to monomer loss is the propagation reaction. We can solve this equation if we have an expression for M*, the free radical chain end concentration. We apply the quasi-steady state assumption in order to approximate M*. QSSA (Quasi-steady state assumption) If we want long chains, we need to have only a few of them reacting at one time. Therefore, we want M* to be small. We design most free radical polymerizations so that M* is much smaller than M. We make the approximation that the change in M* is nearly zero compared to the change in M.
chapter 4. Fall 2011 20
chapter 4. Fall 2011 21
chapter 4. Fall 2011 22
chapter 4. Fall 2011 23
IN-CLASS EXAMPLE
chapter 4. Fall 2011 24
Team Another reaction mechanism
7 Inhibitor added
Fantastic 4 Chain transfer agent
Mountain goats
Plastics anonymous Second initiator
Poly-cats
polymaniacs Thermal initiation
Team alpha
chapter 4. Fall 2011 25
POLY(METHYL VINYL ETHER)A photopolymerization case study
chapter 4. Fall 2011 26
chapter 4. Fall 2011 27
PHOTOINITIATOR DECAY
Objective: use a typical study of photoinitiator decomposition to estimate kd, the dissociation rate constant.
Approach: use a system linked to vinyl ether polymerizations (solvents, monomers, etc. all affect the performance of catalysts, initiators and ionic catalysts)Reference: Cook, et al., Photopolymerization of vinyl ether networks using an iodonium initiator – the role of phototsensitizers, J. Polym. Sci., Part A: Polym. Chem., 47, 5474-87 (2009). Copy on course webpage.System: triethylene glycol divinyl ether; diphenyl iodonium salt, one of three photosensitizers (CPTXO, AO, CQ – not consumed). Note: photosensitizer allows the use of the visible spectrum range rather than UV (which would require quartz windows, etc).
chapter 4. Fall 2011 28
Absorbance change during irradiationspecific wavelengths linked to fct. Groups (Fig. 4)
2 systems
chapter 4. Fall 2011 29
PI rate constants
photoinitiator Kd, s-1
AO 0.0374
CPTXO 0.0209
Polymerization conditions:20 C; TEGDVE – triethylene glycol divinyl ether;60 kJ/mol – heat of polymerization;
chapter 4. Fall 2011 30
chapter 4. Fall 2011 31
Goofy stuffDegradation rate of CPTXO does not follow exponential decay over long times. As suggested on p. 5484, PI process is in competition with a side reaction that quenches CPTXO or with a process that consumes cations (perhaps an impurity).
chapter 4. Fall 2011 32
MVE POLYMERIZATION RATES VS. T
Objective: use a typical study of MVE polymerization vs. T to to estimate Ea, the activation energy of the overall reaction process. This can be used to scale the polymerization rate vs. T for process design purposesApproach: use a system linked to vinyl ether polymerizations (solvents, monomers, etc. all affect the performance of catalysts, initiators and ionic catalysts)Reference: MVE in toluene; diethoxyethane/trimethyl silyl iodide, ZnI2 activator
chapter 4. Fall 2011 33
Semi-batch analysis
Batch analysis of the rate can be done at the end of the monomer feed phaseEach curve is modeled by an ionic polymerization eqn., yielding kp. These are plotted as kp vs. 1/T, and the slope is related to the activation energy.
chapter 4. Fall 2011 34
chapter 4. Fall 2011 35
chapter 4. Fall 2011 36
Polymerization rates
• Polymer Handbook: kp2/kt, • Chen et al.: 1.5 to 2 hours, 30 C, palladium
complex• Sakaguchi et al.: 30 min, -78 C
chapter 4. Fall 2011 37