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Plastics technology. Часть 2. Учебное пособие.pdf
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Figure 54 - Schematic representation of preferential sorption capillary flow mechanism (a). Critical pore diameter for maximum separation and permeability (b)
From an industrial standpoint, the two basic parameters characterizing reverse osmosis systems for a given separation are:
(1) rejection factor, which involves the choice of the appropriate chemical nature of the film surface;
(2) water flux, which depends on methods for preparing films containing the la rg e st num bers of pores of the required size.
This approach is the basis of the successful development of porous cellulose acetate membranes for desalination and other applications.
To achieve high flux in reverse osmosis, the membrane should have a high surface area and be very thin (0.02-1.0 mm), but to withstand the high applied pressure it also needs to be very strong. To meet these requirements, which are in conflict, the semipermeable membrane is used as a skin mounted on a support, which is another membrane that is very porous, like a filter paper, and that is nonselective, and very thick (>100 μm). In some such bilayers each layer is of the same polymer and the membrane is then called integral or asymmetric, but in others the layers are of different polymers and the membrane is called a composite. Composite membranes have the advantage of each layer being individually optimized – the skin for its permeability and the support for its strength – but they are harder to make them integral membranes.
Polyelectrolytes, except those which are covalently cross-linked, are soluble in water, and their applications are based on this property. Basically, these applications depend on the polyelectrolyte altering the fluid properties of an aqueous medium, or modifying the behavior of particles in aqueous slurries or colloidal suspensions.
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Polyelectrolytes raise the viscosity of aqueous solutions thus acting as thickeners, and the magnitude of the effect increases with the polymer’s molecular weight. Naturally occurring gums and acidic polysaccharides have been traditionally used as thickening agents in food stuffs and pharmaceutical products, but, more recently, synthetic polyelectrolytes have been used in these roles. Much use is also made of polyelectrolytes to modify the characteristics of latex paints and similar proprietary fluids.
Polyelectrolytes can also stabilize particles in aqueous suspension and so act as dispersants. In this reaction, the hydrophobic backbones of polyelectrolytes are absorbed onto the surface of the particles by van der Waals attraction, while their ions form a hydrophilic surface and interact with water. In suspension or bead polymerization, for example, a hydrophobic vinyl monomer is dispersed in water by agitation to form droplets that are stabilized by a polyelectrolyte. Each stabilized droplet of the monomer acts as a bulk polymerization system and on polymerization gets the shape of a bead.
Polyelectrolytes, depending on their ionic charge, can interact with colloidal particles and neutralize the stabilizing hydrophilic charges, thus acting as flocculating agents. They have been used in this way to coagulate slurries and industrial wastes.
There are other applications of polyelectrolytes that depend on their behavior in water in various ways. They are thus used as sizes in the textile industry and in paper manufacturing, and as additives to drilling muds and to soil for conditioning purposes.
A very different kind of application of polyelectrolytes is their use as dental cements. Here a divalent cation is added to an aqueous solution of a polyanion to form a highly cross-link ed precip itate o f great strength.
2.5.1 Ionomers
Polyethylene ionomers
Ionomers based on polyethylene are mainly copolymers with pendant carboxylate groups in which the polyethylene backbone is their major component (>90%). Ethylene is directly copolymerized with methacrylic acid in a continuous process developed from the high-pressure method used to make low-density polyethylene by free-radical initiation. The comonomers are mixed in appropriate proportions, allowing for the greater reactivity of the methacrylic acid, and introduced with a peroxide initiator to a reactor at a pressure of about 207 MPa and a temperature of
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250-280°C. Because methacrylic acid reacts disproportionately rapidly and has to be replenished frequently, the conversion to polymer is kept low per pass, and at 15-20% conversion the residual monomer is removed, then recycled with fresh monomer. This ensures that the methacrylic acid units, and hence the ionic cross-l inks formed later, are randomly distributed and uniform in composition.
The distinctive properties of the ionomers become manifest only when the carboxylic acid groups are neutralized. The neutralization is a kind of post-treatment that is performed by melting the polyacid in a mill at 150°C and adding a base or basic salt in powder form or in solution. In these neutralizations, the melt starts as a soft, fluid, opaque mass of polyacid and then becomes stiff, rubbery, and transparent as the ionomer is formed.
The loss in fluidity, or gain in melt strength, is a significant factor determining the usefulness of ionomers. That the effect is due to the formation of strong ionic cross-links is clearly shown by a comparison of the melt viscosity of an ionomer with its acid precursor (Figure 55). The melt viscosity of a cop olymer of eth ylene a nd metha cryli c acid co ntain ing, for example, 2 mole per cent of acid is increased by only about 50% compared to an otherwise equivalent polyethylene homopolymer, but when neutralized, and therefore ionized, the melt viscosity increa ses tw enty-fold. (The slight increase with the acid is attributed to the weak hydrogen­bonded cross-links.) The melt-strength of an ionomer is such that its molten film can be drawn over the sharp edges of a nail without it being punctured or torn.
A striking property of the ethylene ionomers is that they are transparent, unlike their acid precursors or polyethylene itself, which are not. The haze in polyethylene is due to the fact that the polymer is partially crystalline, and minute crystallites within it agglomerate into spherulites, which are of a size to scatter light. Ionomers also contain crystallites, and the crystallite formation is, in fact, helped by the ions, the domains of which serve to nucleate them; but the crystallites are unable to agglomerate because of the high viscosity of their surroundings. Thus, microcrystallinity is enhanced by the ions, but macro-crystallinity, which causes haze, is inhibited. The transparency of ionomers is useful in packaging applications.
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Figure 55 - Melt viscosity of poly(ethylene-co-methacrylic acid)
Copolymer*
Ionomer
Na+ Zn
2+
Appearance
Tensile strength, MPa
Hazy
12.4
Hazy
23.4
Transparent
35.9
Transparent
29.6
and its sodium salt relative to polyethylene.
Some physical properties of polyethylene ionomers are compared with those of polyethylene and the acid copolymer, poly(ethylene-co­methacrylic acid) in Table 21. Ionomer is generally tougher and, as shown in Table 21, relative to the acid copolymer, its tensile strength is increased by 27-53% and its stiffness is nearly tripled.
Table 21 – Comparative physical properties of polyethylene ionomers and their acid precursor
Property PE
Melt index, g/10 min Elongation, %
Polyethylene ionomers are described as flexible and tough with good impact toughness at low temperature, and with good resistance to grease and solvents, to stress-cracking, and to abrasion. They are blow­molded into films, sheets, bottles, and blister packs, and injection-molded into various objects. Their resistance to grease and solvents has made them useful in meat packaging. They are very effective as external coatings on glass bottles to contain break ag es.
-
600
(–CO2H)
5.8
553
0.03 330
0.09 313
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Elastomeric ionomers
A number of ionic polymers exist that have a recognized elastomer as the covalent backbone and have a small ionic content, so they may be called elastomeric ionomers. The ions provide at least a part of the cross­links in these polymers. Those elastic ionomers that are cross-linked exclusively by their ions have, however, the useful feature of being thermoplastic.
Carboxylated polybutadiene ionomers, which are close relatives of the polyethylene ionomers described above, have an essentially polybutadiene backbone that contains some acrylonitrile and styrene to adjust its flexibility and toughness, and, in addition, up to 6% by weight of acrylic or methacrylic acid. Like the polyethylene ionomers, they are usually made by direct copolymerization with the carboxylic acid monomer using, however, emulsion methods. Typically the monomers are slurried in water with sodium dodecylbenzene sulfonate as the emulsifier and potassium persulfate as the free-radical initiator. The tendency of the carboxylic acid monomer to dissolve in the aqueous phase instead of remaining in the butadiene-rich phase is suppressed by making the aqueous phase acidic so that the monomer remains in the nonionized form.
The carboxylated polybutadienes, when neutralized, undergo ionic cross-linking, producing the effect of vulcanization. The neutralization can be done by treating with aqueous sodium hydroxide then heating, or by heating directly with zinc oxide. The ionic cross-link formed with the sodium ion of moderate strength at room temperature and dissociates at 100°C. With zinc, the ionic cross-link formed is much stronger, although the polymer is capable of substantial flow at higher temperatures.
Some properties of sodium and zinc vulcanizates are compared with those of the acid precursor in Table 22. High tensile strength is a characteristic of ionic vulcanizates. As a comparison, a standard polybutadiene elastomer vulcanized with sulfur gives a strength of 1.9-5.8 MPa, whereas an equivalent copolymer containing 1.5 mole% methacrylic acid, and vulcanized with magnesium oxide, gives 29.0 MPa. They also respond differently to fillers such as carbon black – sulfur vulcanizates are reinforced, while ionic vulcanizates are weakened.
Carboxylated polybutadienes have not been used much as thermoplastic elastomers, principally because they have poor compression set, high stress relaxation, and poor performance at higher temperatures. Carboxylated polybutadienes, supplied as lattices, are used mainly in
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dipping and coating processes, applications, which often do not involve
Property
Acid
copolymer
Sodium
vulcanizate
Zinc
vulcanizate
Tensile strength, MPa
0.7
11.7
41.4
ionized carboxylate, at least directly. The applications include adhesives, paper coating, glove-dipping, carpet-backing, binding nonwoven fabrics, and also shrink-proofing woolen garments where the carboxyl groups are believed to react with pendant amino groups in the proteins of the wool. A wide range of carboxylated lattices are available as well-developed items of commerce; some of these are styrene-butadiene rubbers (SBRs) and others are acrylonitrile-butadiene rubbers (NBRs).
Table 22 – Vulcanization of carboxylated polybutadienes
Elongation, %
1600
900
400
Mixed vulcanizations, such as with zinc oxide and sulfur or zinc oxide and peroxide, are used for carboxylated NBRs in order to combine the advantages of the ionic method with the conventional methods. The mixed vulcanizates have high tensile strength and notable resistance to abrasion, oil, and fuel. They are used in applications such as industrial rollers and wheels and shoe soles. Dry NBRs are available in fewer grades than lattices. Examples are Krynac by Doverstrand and Hycar by Goodrich.
Elastomeric ionomers have also been developed from ethylene­propylene-diene ternary copolymers known as EPDM rubbers. The diene is commonly ethylidene norbornene. Du Pont made carboxylated ionomers by free-radical grafting of maleic anhydride (0.5-5%) onto the die ne moi et y of the polymer and neutralized the product with rosin salt. The ethylidene norbornene can also be sulfonated, thus:
Ionomer properties of sulfonated EPDM are said to develop only
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when the acids are neutralized. The best properties are given by zinc salts, particularly when they are plasticized by zinc stearate.
Ionomers based on polytetrafluoroethylene
Polymers with a polytetrafluoroethylene (PTFE) backbone and pendant perfluorosulfonate or perfluorocarboxylate groups have become commercially important materials, although they are expensive. The sulfonates were introduced as Nafion by Du Pont in the early 1970s and the carboxylates as Flemion by Asahi Glass in 1978. They are made by free­radical copolymerization of tetrafluoroethylene and perfluorovinyl monomers giving precursor copolymers, (1) and (2), which can be post­functionalized by hydrolysis to generate sulfonic and carboxylic acid groups. The perfluorovinyl monomers themselves are made from tetrafluoroethylene by multi-step synthesis using hexafluoropropylene oxide.
Nafion precursor Flemion precursor
(1) (2)
Although originally developed for use as a membrane in fuel cells, Nafion has found more useful applications in various other electrolytic separation processes. In these applications, use is made of its cation­exchange properties and its ability to survive in extremely aggressive chemical environments. An outstanding example is the use of Nafion as a membrane in the chlor-alkali cell where it is gradually replacing the traditional diaphragm and mercury cells. In the chlor-alkali process a cell is partitioned by the polyanionic membrane into an anode compartment, to which brine is added, and a cathode compartment to which water is added (Figure 56). On application of electric potential, Na+ passes from the brine around the anode and through the membrane to the water around the cathode where it forms sodium hydroxide. The membrane keeping the brine and water separate allows transfer of Na+ ions by ion-exchange and acts as a barrier to Cl– and OH–.
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Figure 56 - Chlor-alkali cell
The Nafion membranes have ionic contents of 0.66-0.91 Eq/kg. A bilayer of these two extremes of composition is made and also a bilayer with a perfluorocarboxylate (Flemion) polymer. The bilayered membranes are made by melt processing the precursor copolymer, which then, in membrane form, is hydrolyzed.
Perfluorocarboxylates, the Flemions, were introduced with the idea that a carboxylate at a given ion content would be less hydrophilic than a sulfonate and so would be of help in balancing the ionic content of an ion­exchange membrane with its permselectivity and hydrophilicity as required. The bilayered Nafions also resulted from similar thinking and at tempt to combine certain advantages of the two types.
The efficiency with which power is consumed in the electrolysis and the highest concentration of uncontaminated sodium hydroxide that can be produced determine the membrane performance in the chlor-alkali process. Rapid progress in membrane performance has been made since the introduction of carboxylate membranes, leading to an efficiency level of 95% and a concentration of 33%.
Bilayer carboxylate membranes can be produced by surface modification of Nafion-type membranes. In a process used by Asahi Chemical the sulfonate on a Nafion-type surface is reduced to sulfinic and sulfenic acids, then oxidized to a carboxylate layer of 2-10 mm thickness:
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Tokoyama Soda makes Neosepta F membranes by treating a Nafion-type precursor with an alcohol and the oxidizing the surface in air.
Nafions in their acid forms are super-acidic, i.e., stronger than sulfuric acid and so have high catalytic power. Nafion powders in acid form have therefore been used as catalysts in many types of reactions, such as esterification and Friedel-Crafts reactions at low temperatures.
Ionomers based on polysulfones
Ionomers of commercial polysulfones, principally sulfonates, are being developed as membranes, particularly for purifying water by reverse osmosis. In this application, they are superior to conventional membrane materials because they are resistant to oxidation by the chlorine used in water treatment, to harsh chemical cleaning operations, to biological fouling, and to compaction under high operating pressures. The traditional polymer, cellulose acetate, is less strong, while Nafion, though very inert chemically, is too costly and difficult to fabricate in a form suitable for reverse osmosis. The sulfones, having completely amorphous backbones and solubility, can be easily cast into membranes from solvents. The optimum ion content is about one eq/kg, which provides a balance of properties between a high flux of the permeant (water) and a low leakage of the rejected species (the dissolved salts).
Commercial polysulfones such as Udel (Union Carbide) and Victrex (ICI) are sulfonated in a post-functionalization step to make ionomers. When dissolved in dichloroethane and treated with a complex of sulfur trioxide and triethyl phosphate, Udel becomes monosulfonated on the rings marked R (as the rings connected to the sulfone group are deactivated by the sulfone group):
Udel
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Victrex is a random copolymer of two units in which the ring marked R of unit B becomes monosulfonated by the simple process of dissolving it in sulfuric acid. The other aromatic rings and the whole of unit A are inert. The extent of the reaction is predetermined by the proportion of unit B in the copolymer. The strength of the ionic associations in sulfonated Victrex is indicated by the increase in Tg, which occurs linearly with the content of unit B despite the already high value of 230°C for the parent polymer.
Victrex

2.5.2 Polyelectrolytes

Ion-exchangers
The most important class of ion-exchangers are the organic ion­exchange resins. Their framework, the so-called matrix, consists of an irregular, macromolecular, three-dimensional network of hydrocarbon chains. The matrix carries ionic groups such as –SO AsO
2–
in cation exchangers and –NH
3
+
, >NH
3
, –COO–, –PO
3
+
, >N+<, and S+ in anion
2
2–
3
, and
exchangers. Ion-exchange resins thus are cross-linked polyelectrolytes. The first completely synthetic ion-exchange resins were prepared by B.A.Adams and E.C.Holmes in England in 1935. Today more than 100 synthetic ion-exchange resins are marketed throughout the world by various companies.
Ion-exchange resins are supplied as insoluble, water-swellable beads that have either a dense internal structure (gel-type) or a porous, multichannelled one (macroporous-type or macroreticular). The gel-type PS resin was the first to be introduced (1947) and the macroporous-type came later (1959).
Ion-exchangers are broadly classified as cation exchangers and anion-exchangers. Carriers of exchangeable cations are called cation