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| [[File:Step-growth polymerization.jpg|thumbnail|A generic representation of a step-growth polymerization. (Single white dots represent monomers and black chains represent oligomers and polymers)<ref name=Cowie />]]
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| [[File:Comparison between SG and CG.jpg|thumbnail|200px|right|Comparison of Molecular weight vs conversion plot between step-growth and [[living polymerization|living]] chain-growth polymerization]]
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| '''Step-growth polymerization''' refers to a type of [[polymerization]] mechanism in which bi-functional or multifunctional [[monomers]] react to form first [[Dimer (chemistry)|dimers]], then [[trimer (chemistry)|trimers]], longer [[oligomers]] and eventually long chain [[polymers]]. Many naturally occurring and some synthetic polymers are produced by step-growth polymerization, e.g. [[polyester]]s, [[polyamide]]s, [[polyurethane]]s, etc. Due to the nature of the polymerization mechanism, a high extent of reaction is required to achieve high molecular weight. The easiest way to visualize the mechanism of a step-growth polymerization is a group of people reaching out to hold their hands to form a human chain — each person has two hands (= reactive sites). There also is the possibility to have more than two reactive sites on a monomer: In this case branched polymers are produced.
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| ==Step growth polymerisation and condensation polymerization==
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| "Step growth polymerisation" and '''condensation polymerization''' are two different concepts, not always identical. In fact [[polyurethane]] polymerizes with addition polymerization (because its polymerization produces no small molecules), but its [[reaction mechanism]] corresponds to a step-growth polymerization.
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| The distinction between "addition polymerization" and "condensation polymerization" was introduced by [[Wallace Hume Carothers]] in 1929, and refers to the type of products, respectively:<ref>{{cite journal | doi=10.1021/ja01383a041 | author=W. H. Carothers | title= | journal = Journal of American Chemical Society | year = 1929 | volume = 51 | issue = 8| pages=2548 }}</ref><ref>Paul J. Flory, [http://books.google.com/books?id=CQ0EbEkT5R0C&pg=PA37&lpg=PA37&dq=Carothers+polymer+addition+condensation&source=bl&ots=13v-5Uxvju&sig=h1RcDqB_plK0WR__xwxwjuLybC4&hl=it&ei=wdJUSuKSKY2angPIt4SMDA&sa=X&oi=book_result&ct=result&resnum=1 "Principles of Polymer Chemistry"], Cornell University Press, 1953, p.39. ISBN 0-8014-0134-8</ref>
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| * a polymer only (addition)
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| * a polymer and a molecule with a low molecular weight (condensation)
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| The distinction between "step-growth polymerization" and "chain-growth polymerization" was introduced by [[Paul Flory]] in 1953, and refers to the [[reaction mechanism]]s, respectively:<ref>Susan E. M. Selke, John D. Culter, Ruben J. Hernandez, [http://books.google.com/books?id=1aM9n0hovOoC&dq=Flory+polymer+addition+condensation&hl=it "Plastics packaging: Properties, processing, applications, and regulations"], Hanser, 2004, p.29. ISBN 1-56990-372-7</ref>
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| * by functional groups (step-growth polymerization)
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| * by free-radical or ion (chain-growth polymerization)
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| ==Branched polymers==
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| A monomer with functionality of 3 or more will introduce '''branching''' in a polymer and will ultimately form a [[cross-link]]ed macrostructure or network even at low fractional conversion. The point at which this three-dimensional structure is formed is known as the [[gel point]] because it is signalled by an abrupt change in [[viscosity]]. One of the earliest so-called [[thermoset]]s is known as [[bakelite]]. It is not always water that is released in step-growth polymerization: in [[acyclic diene metathesis]] or ADMET dienes polymerize with loss of [[ethylene]].
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| ==Differences between step-growth polymerization and chain-growth polymerization==
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| This technique is usually compared with [[chain-growth polymerization]] to show its characteristics.
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| {|class="wikitable" style="text-align:center"
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| |-
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| !'''Step-growth polymerization'''!!'''Chain-growth polymerization'''
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| |-
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| |Growth throughout matrix||Growth by addition of monomer only at one end of chain
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| |-
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| |Rapid loss of monomer early in the reaction||Some monomer remains even at long reaction times
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| |-
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| |Similar steps repeated throughout reaction process||Different steps operate at different stages of mechanism (i.e. Initiation, propagation and termination)
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| |-
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| |Average molecular weight increases slowly at low conversion and high extents of reaction are required to obtain high chain length||Molar mass of backbone chain increases rapidly at early stage and remains approximately the same throughout the polymerization
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| |-
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| |Ends remain active (no termination)||Chains not active after termination
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| |-
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| |No initiator necessary||Initiator required
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| |-
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| |}
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| ==Historical Aspects==
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| Most natural polymers being employed at early stage of human society are of condensation type. The synthesis of first truly synthetic polymeric material, [[Bakelite]], was announced by [[Leo Baekeland]] in 1907, through a typical step-growth polymerization fashion of [[phenol]] and [[formaldehyde]].
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| The pioneer of synthetic polymer science, [[Wallace H. Carothers]], developed a new means of making [[polyesters]] through step-growth polymerization in 1930s as a research group leader at [[DuPont]]. It was the first reaction designed and carried out with the specific purpose of creating high molecular weight polymer molecules, as well as the first polymerization reaction whose results had been predicted beforehand by scientific theory. Carothers developed a series of mathematic equations to describe the behavior of step-growth polymerization systems which are still known as the Carothers equations today. Collaborating with [[Paul J. Flory]], who is a physical chemist, they developed theories that describe more mathematical aspects of step-growth polymerization including kinetics, stoichiometry, and molecular weight distribution etc. Carothers is also well known for his invention of [[Nylon]].
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| == Classes of step-growth polymers <ref name=seymour>{{cite book
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| | last = Seymour
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| | first = Raymond
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| | title = Polymer Chemistry An Introduction
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| | publisher = Marcel Dekker, Inc.
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| | isbn = 0-8247-8719-6
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| | year = 1992}}</ref><ref>H.F. Mark, N. M. B., C. G. Overberger, G. Menges, Encyclopedia of Polymer Science and Engineering Wiley-Interscience: New York, 1988.</ref>==
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| *[[Polyester]] has high [[glass transition]] temperature T<sub>g</sub> and high [[melting point]] T<sub>m</sub>, good mechanical properties to about 175 °C, good resistance to solvent and chemicals. It can exist as fibers and films. The former is used in garments, felts, tire cords, etc. The latter appears in magnetic recording tape and high grade films.
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| *[[Polyamide]] ([[nylon]]) has good balance of properties: high strength, good elasticity and abrasion resistance, good toughness, favorable solvent resistance. The applications of polyamide include: rope, belting, fiber cloths, thread, substitute for metal in bearings, jackets on electrical wire.
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| *[[Polyurethane]] can exist as [[elastomers]] with good abrasion resistance, hardness, good resistance to grease and good elasticity, as fibers with excellent rebound, as coatings with good resistance to solvent attack and abrasion and as foams with good strength, good rebound and high impact strength.
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| *[[Polyurea]] shows high T<sub>g</sub>, fair resistance to greases, oils, and solvents. It can be used in truck bed liners, bridge coating, caulk and decorative designs.
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| *[[Polysiloxane]] are available in a wide range of physical states—from liquids to greases, [[waxes]], [[resins]], and [[rubbers]]. Uses of this material are as antifoam and release agents, gaskets, seals, cable and wire insulation, hot liquids and gas conduits, etc.
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| *[[Polycarbonates]] are transparent, self-extinguishing materials. They possess properties like crystalline [[thermoplasticity]], high impact strength, good thermal and oxidative stability. They can be used in machinery, auto-industry, and medical applications. For example, the [[cockpit canopy]] of [[F-22 Raptor]] is made of high optical quality polycarbonate.
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| *[[Polysulfides]] have outstanding oil and solvent resistance, good gas impermeability, good resistance to aging and [[ozone]]. However, it smells bad, and it shows low tensile strength as well as poor heat resistance. It can be used in gasoline hoses, gaskets and places that require solvent resistance and gas resistance.
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| *[[Polyether]] shows good thermoplastic behavior, water solubility, generally good mechanical properties, moderate strength and stiffness. It is applied in sizing for cotton and synthetic fibers, stabilizers for adhesives, binders, and film formers in pharmaceuticals.
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| *[[Phenol formaldehyde resin]] ([[Bakelite]]) have good heat resistance, dimensional stability as well as good resistance to most solvents. It also shows good [[dielectric]] properties. This material is typically used in molding applications, electrical, radio, televisions and automotive parts where their good dielectric properties are of use. Some other uses include: impregnating paper, varnishes, decorative laminates for wall coverings.
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| ==Kinetics==
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| <!-- show mech? --> | |
| The kinetics and rates of step-growth polymerization can be described using a polyesterification mechanism. The simple esterification is an acid-catalyzed process in which protonation of the acid is followed by interaction with the alcohol to produce an ester and water. However, there are a few assumptions needed with this kinetic model. The first assumption is water (or any other condensation product) is efficiently removed. Secondly, the functional group reactivities are independent of chain length. Finally, it is assumed that each step only involves one alcohol and one acid. | |
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| :<math>\frac{1}{1-p^{n-1}}=1+(n-1)kt[COOH]^{n-1}</math>
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| This is a general rate law degree of polymerization for polyesterification
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| where n= reaction order.
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| ===Self-catalyzed polyesterification=== | |
| If no acid catalyst is added, the reaction will still proceed because the acid can act as its own catalyst. The rate of condensation at any time t can then be derived from the rate of disappearance of -COOH groups and
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| :<math>rate=\frac{-d[COOH]}{dt}=k[COOH]^2[OH]</math>
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| The second-order [COOH] term arises from its use as a catalyst, and k is the rate constant. For a system with equivalent quantities of acid and glycol, the functional group concentration can be written simply as
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| :<math>rate=\frac{-d[COOH]}{dt}=k[COOH]^3</math>
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| After integration and substitution from [[Carothers equation]], the final form is the following
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| :<math>\frac{1}{(1-p)^2}=2kt[COOH]^2+1=X^2_n</math>
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| For a self-catalyzed system, the '''number average degree of polymerization''' (Xn) grows proportionally with <math>\sqrt(t)</math>.<ref name=Yves>Yves Gnanou; Fontanille, M., Organic and Physical Chemistry of Polymers.</ref>
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| ===External catalyzed polyesterification===
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| The uncatalyzed reaction is rather slow, and a high X<sub>n</sub> is not readily attained. In the presence of a catalyst, there is an acceleration of the rate, and the kinetic expression is altered to<ref name=Cowie>Cowie, J.M.G; Arrighi, V., Polymers: Chemistry and Physics of Modern Materials. 3 ed.; CRC Press: 2008.</ref>
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| :<math>\frac{-d[COOH]}{dt}=k[COOH][OH]</math>
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| which is kinetically first order in each functional group. Hence,
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| :<math>\frac{-d[COOH]}{dt}=k[COOH]^2</math>
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| and integration gives finally
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| :<math>\frac{1}{1-p}=1+[COOH]kt=X_n</math>
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| For an externally catalyzed system, the number average degree of polymerization grows proportionally with <math>t\,</math>.
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| ==Molecular weight distribution in linear polymerization<ref name=flory>{{cite book
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| | last = Flory
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| | first = Paul
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| | title = Principles of Polymer Chemistry
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| | publisher = Cornell University Press
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| | pages = 321–322
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| | isbn = }}</ref>==
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| The product of a polymerization is a mixture of polymer molecules of different molecular weights. For theoretical and practical reasons it is of interest to discuss the distribution of molecular weights in a polymerization. The '''[[molecular weight distribution]] (MWD)''' had been derived by Flory by a statistical approach based on the concept of equal reactivity of functional groups.<ref name=Odian>{{cite book
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| | last = Odian
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| | first = George
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| | title = Principles of polymerization
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| | publisher = John Wiley& Sons, INC
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| | year = 1991
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| | isbn = 0-471-61020-8}}</ref>
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| ===Probability===
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| Step-growth polymerization is a random process so we can use statistics to calculate the probability of finding a chain with x-structural units ("x-mer") as a function of time or conversion.
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| :<math>xAA + xBB \rightarrow AA-(BB-AA)_{x-1}-BB</math>
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| :<math>xAB \rightarrow A-(B-A)_{x-1}-B</math>
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| Probability that an 'A' functional group has reacted
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| :<math>p^{x-1} \,</math>
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| Probability of finding an 'A' unreacted
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| :<math>(1-p) \,</math>
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| Combining the above two equations leads to.
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| :<math>P_x=(1-p)p^{x-1} \,</math>
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| Where P<sub>x</sub> is the probability of finding a chain that is x-units long and has an unreacted 'A'. As x increases the probability decreases.
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| ===Number fraction distribution<ref>{{cite journal
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| | last = Stockmayer
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| | first = Waters
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| | authorlink =
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| | coauthors =
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| | title = Molecular distribution in condensation polymers
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| | journal = Journal of polymer science
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| | volume = IX
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| | issue = 1
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| | pages = 69–71
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| | publisher =
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| | location =
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| | year = 1952
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| | url =
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| | doi = 10.1002/pol.1952.120090106
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| | id =
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| | accessdate = |bibcode = 1952JPoSc...9...69S }}</ref>=== | |
| [[File:Number fraction.jpg|thumb|200px|Number-fraction distribution curve for linear polymerization. Plot 1, p=0.9600; plot 2, p=0.9875; plot 3, p=0.9950.]] | |
| The '''number fraction distribution''' is the fraction of x-mers in any system and equals the probability of finding it in solution.
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| :<math>\frac{N_x}{N}=(1-p)p^{x-1} \,</math>
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| Where N is the total number of polymer molecules present in the reaction.
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| ===Weight fraction distribution<ref name=Cowie/>===
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| [[File:Weight fraction.jpg|thumb|200px|Weight fraction distribution plot for linear polymerization. Plot 1, p=0.9600; plot 2, p=0.9875; plot 3, p=0.9950.]]
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| The '''weight fraction distribution''' is the fraction of x-mers in a system and the probability of finding them in terms of mass fraction.
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| :<math>\frac{W_x}{W_o}=\frac{xN_xM_o}{N_oM_o}=\frac{xN_x}{N_o}=x\frac{N_x}{N}\frac{N}{N_o}</math>
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| Notes:
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| :* ''M<sub>o</sub>'' is the molar mass of the [[repeat unit]],
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| :* ''N<sub>o</sub>'' is the initial number of monomer molecules,
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| :* and ''N'' is the number of unreacted functional groups
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| Substituting from the [[Carothers equation]]
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| :<math>X_n=\frac{1}{1-p}=\frac{N_o}{N}</math>
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| We can now obtain:
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| :<math>\frac{W_x}{W_o}=x(1-p)^2p^{x-1} \,</math>
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| | |
| ===PDI===
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| The '''[[polydispersity index]] (PDI)''', is a measure of the distribution of molecular mass in a given polymer sample.
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| :<math>PDI=\frac{M_w}{M_n}</math>
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| However for step-growth polymerization the [[Carothers equation]] can be used to substitute and rearrange this formula into the following.
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| :<math>PDI=1+p \,</math>
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| Therefore, in step-growth when p=1, then the PDI=2.
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| | |
| ==Molecular weight control in linear polymerization==
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| ===Need for stoichiometric control===
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| There are two important aspects with regard to the control of molecular weight in polymerization. In the synthesis of polymers, one is usually interested in obtaining a product of very specific molecular weight, since the properties of the polymer will usually be highly dependent on molecular weight. Molecular weights higher or lower than the desired weight are equally undesirable. Since the degree of polymerization is a function of reaction time, the desired molecular weight can be obtained by quenching the reaction at the appropriate time. However, the polymer obtained in this manner is unstable in that it leads to changes in molecular weight because the ends of the polymer molecule contain functional groups that can react further with each other.
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| This situation is avoided by adjusting the concentrations of the two monomers so that they are slightly nonstoichiometric. One of the reactants is present in slight excess. The polymerization then proceeds to a point at which one reactant is completely used up and all the chain ends possess the same functional group of the group that is in excess. Further polymerization is not possible, and the polymer is stable to subsequent molecular weight changes.
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| Another method of achieving the desired molecular weight is by addition of a small amount of monofunctional monomer, a monomer with only one functional group. The monofunctional monomer, often referred to as a chain stopper, controls and limits the polymerization of bifunctional monomers because the growing polymer yields chain ends devoid of functional groups and therefore incapable of further reaction.<ref name=Odian />
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| ===Quantitative aspects===
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| To properly control the polymer molecular weight, the stoichiometric imbalance of the bifunctional monomer or the monofunctional monomer must be precisely adjusted. If the nonstoichiometric imbalance is too large, the polymer molecular weight will be too low. It is important to understand the quantitative effect of the stoichiometric imbalance of reactants on the molecular weight. Also, this is necessary in order to know the quantitative effect of any reactive impurities that may be present in the reaction mixture either initially or that are formed by undesirable side reactions. Impurities with A or B functional groups may drastically lower the polymer molecular weight unless their presence is quantitatively taken into account.<ref name=Odian />
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| More usefully, a precisely controlled stoichiometric imbalance of the reactants in the mixture can provide the desired result. For example, an excess of diamine over an acid chloride would eventually produce a polyamide with two amine end groups incapable of further growth when the acid chloride was totally consumed. This can be expressed in an extension of the [[Carothers equation]] as,
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| :<math>X_n=\frac{(1+r)}{(1+r-2rp)}</math>
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| were r is the ratio of the number of molecules of the reactants.
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| :<math>r=\frac{N_{AA}}{N_{BB}}</math> were N<sub>BB</sub> is the molecule in excess.
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| The equation above can also be used for a monofunctional additive which is the following,
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| :<math>r=\frac{N_{AA}}{(N_{BB}+2N_B)}</math>
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| where N<sub>B</sub> is the number of monofunction molecules added. The coefficient of 2 in front of N<sub>B</sub> is require since one B molecule has the same quantitative effect as one excess B-B molecule.<ref name=Stevens>{{cite book
| |
| | last = Stevens
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| | first = Malcolm
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| | title = Polymer Chemistry An Introduction
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| | publisher = Oxiford University Press
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| | year = 1990
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| | isbn = 019505759}}</ref>
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| ==Multi-chain polymerization==
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| A monomer with '''functionality''' 3 has 3 functional groups which participate in the polymerization. This will introduce [[branching (chemistry)|branching]] in a polymer and may ultimately form a [[cross-linked]] macrostructure. The point at which this three-dimensional network is formed is known as the [[gel point]], signaled by an abrupt change in viscosity.
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| A more general functionality factor f<sub>av</sub> is defined for multi-chain polymerization, as the average number of functional groups present per monomer unit. For a system containing N<sub>0</sub> molecules initially and equivalent numbers of two function groups A and B, the total number of functional groups is N<sub>0</sub>f<sub>av</sub>.
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| : <math>f_{av} = \frac{\sum N_i \sdot f_i}{\sum N_i}</math>
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| And the '''modified Carothers equation''' is<ref>{{cite journal
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| | last = Carothers
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| | first = Wallace
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| | title = Polymers and polyfunctionality
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| | journal =Transaction of the Faraday Society
| |
| | issue =
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| | pages = 39–49
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| | publisher =
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| | location =
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| | year = 1936
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| | url =
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| | doi = 10.1039/TF9363200039
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| | id =
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| | accessdate =
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| | volume = 32 }}</ref>
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| : <math>x_{n} = \frac{2}{2-pf_{av}}</math>, where p equals to <math>\frac{2(N_0-N)}{N_0 \sdot f_{av}}</math>
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| == Advances in step-growth Polymers <ref>{{cite book
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| | last = Rogers
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| | first = M. E.
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| | authorlink =
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| | coauthors = Long, T. E. Turners, S. R.
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| | title = Synthetic methods in step-growth polymers
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| | publisher = Wiley-Interscience
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| | date =
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| | location =
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| | pages =
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| | url =
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| | doi =
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| | id =
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| | isbn = }}</ref>==
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| The driving force in designing new polymers is the prospect of replacing other materials of construction, especially metals, by using lightweight and heat-resistant polymers. The advantages of lightweight polymers include: high strength, solvent and chemical resistance, contributing to a variety of potential uses, such as electrical and engine parts on automotive and aircraft components, coatings on cookware, coating and circuit boards for electronic and microelectronic devices, etc. Polymer chains based on aromatic rings are desirable due to high bond strengths and rigid polymer chains. High molecular weight and crosslinking are desirable for the same reason. Strong dipole-dipole, hydrogen bond interactions and [[crystallinity]] also improve heat resistance. To obtain desired mechanical strength, sufficiently high molecular weights are necessary, however, decreased solubility is a problem. One approach to solve this problem is to introduce of some flexibilizing linkages, such as isopropylidene, C=O, and {{chem|SO|2}} into the rigid polymer chain by using an appropriate monomer or comonomer. Another approach involves the synthesis of reactive telechelic oligomers containing functional end groups capable of reacting with each other, polymerization of the oligomer gives higher molecular weight, referred to as chain extension.
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| ===Aromatic polyether===
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| [[File:Aromatic polyether.jpg|thumbnail|300px|right]]
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| The oxidative coupling polymerization of many 2,6-disubstituted [[phenols]] using a catalytic complex of a cuprous salt and [[amine]] form aromatic [[polyethers]], commercially referred to as [[poly(p-phenylene oxide)]] or PPO. Neat PPO has little commercial uses due to its high melt viscosity. Its available products are blends of PPO with high-impact [[polystyrene]] (HIPS).
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| ===Polyethersulfone===
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| [[File:Polyethersulfone.jpg|thumbnail|400px|right]]Polyethersulfone (PES) is also referred to as polyetherketone, [[polysulfone]]. It is synthesized by nucleophilic aromatic substitution between aromatic dihalides and bisphenolate salts. Polyethersulfones are partially crystalline, highly resistant to a wide range of aqueous and organic environment. They are rated for continuous service at temperatures of 240-280 °C. The polyketones are finding applications in areas like automotive, aerospace, electrical-electronic cable insulation.
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| ===Aromatic polysulfides===
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| [[File:Polysulfide.jpg|thumbnail|300px|right]]
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| Poly(p-phenylene sulfide) (PPS) is synthesized by the reaction of [[sodium sulfide]] with [[''p''-dichlorobenzene]] in a polar solvent such as 1-methyl-2-pyrrolidinone (NMP). It is inherently flame-resistant and stable toward organic and aqueous conditions; however, it is somewhat susceptible to oxidants. Applications of PPS include automotive, microwave oven component, coating for cookware when blend with [[fluorocarbon polymers]] and protective coatings for valves, pipes, electromotive cells, etc.<ref>{{cite book
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| | last = Walton
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| | first = David
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| | coauthors = Phillip, Lorimer
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| | title = Polymers
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| | publisher = Oxford Univ Pr on Demand
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| | isbn = 0-19-850389-X
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| | year = 2000}}</ref>
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| ===Aromatic polyimide===
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| [[File:Aromatic polyimide.jpg|thumbnail|500px|right]]
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| Aromatic polyimides are synthesized by the reaction of dianhydrides with diamines, for example, pyromellitic anhydride with [[P-phenylenediamine|''p''-phenylenediamine]]. It can also be accomplished using diisocyanates in place of diamines. Solubility considerations sometimes suggest use of the half acid-half ester of the dianhydride, instead of the dianhydride itself. Polymerization is accomplished by a two-stage process due to the insolubility of polyimides. The first stage forms a soluble and fusible high-molecular-weight poly(amic acid) in a polar aprotic solvent such as NMP or [[N,N-dimethylacetamide]]. The poly(amic aicd) can then be processed into the desired physical form of the final plymer product (e.g., film, fiber, laminate, coating) which is insoluble and infusible.
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| ===Telechelic oligomer approach===
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| [[Telechelic]] [[oligomer]] approach applies the usual polymerization manner except that one includes a monofunctional reactant to stop reaction at the oligomer stage, generally in the 50-3000 molecular weight. The monofunctional reactant not only limits polymerization but end-caps the oligomer with functional groups capable of subsequent reaction to achieve curing of the oligomer. Functional groups like [[alkyne]], [[norbornene]], [[maleimide]], [[nitrite]], and [[cyanate]] have been used for this purpose. Maleimide and norbornene end-capped oligomers can be cured by heating. Alkyne, nitrile, and cyanate end-capped oligomers can undergo [[cyclotrimerization]] yielding aromatic structures.
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| ==See also==
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| *[[liquid crystal polymer]]
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| *[[conducting polymer]]
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| *[[Thermosetting plastic]]
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| *[[fire-safe polymers]]
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| ==External links==
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| *[http://www.pslc.ws/macrog/xlink.htm Crosslinking]
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| *[http://www.chemheritage.org/educationalservices/nylon/other/step/step.html The Chemical Heritage Foundation]
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| | |
| ==References==
| |
| {{reflist}}
| |
| | |
| {{DEFAULTSORT:Step-Growth Polymerization}}
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| [[Category:Polymerization reactions]]
| |
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