1. Field of the Invention
The present technique relates generally to elastomeric polyphenylene sulfide (PPS) compositions with improved flexibility properties relative to PPS. In particular, the present technique relates to elastomeric PPS compositions that are useful as a flexible coating, fiber, or barrier.
2. Description of the Related Art
This section is intended to introduce the reader to various aspects of art which may be related to various aspects of the present invention that are described and/or claimed below. This discussion is believed to be helpful in providing the reader with background information to facilitate a better understanding of the various aspects of the present invention. Accordingly, it should be understood that these statements are to be read in this light, and not as any indication of what subject matter may constitute prior art to the present invention.
Thermoplastic polymers, such as plastics and other polymers which may be molded or shaped when heated but which harden in the desired shape when cooled, are commonly incorporated into commercial and manufacturing goods and packages. Particular thermoplastic materials typically vary in their characteristics, such as their flame resistance, impact resistance, flexibility, chemical resistance, heat tolerance, and so forth. As a result, suitable thermoplastic materials are generally selected for an application based upon the demands or constraints of the application. Occasionally, however, a thermoplastic material that might otherwise be well suited for an application may be unacceptable because of an unsuitable characteristic.
For example, polyphenylene sulfide (PPS) is a high-performance engineering thermoplastic with good thermal stability, dimensional stability, chemical resistance, flame resistance, and which is electrically non-conductive. However, PPS may be too inflexible or stiff for some applications in which a high degree of flexibility, resilience, or impact resistance are desired. For example, the stiffness of PPS would generally preclude its use as a coating for substrates which must be bendable or conformable, such as for wires or cables, or as a component in the construction of containers or other articles which must be resistant to impact damage.
However, a PPS-based composition that was sufficiently flexible, resilient, or impact resistant and which possessed the other desirable qualities of PPS might be desirable for such uses. In particular, a PPS-based composition having greater flexibility and/or impact damage resistance relative to pure PPS is highly desirable. Similarly, articles or goods incorporating such a composition, either as a coating or as a structural component are highly desired.
Advantages of the invention may become apparent upon reading the following detailed description and upon reference to the drawings in which:
A. Introduction
Thermoplastic blends based on polyphenylene sulfide (PPS) may be used in a variety of manufacturing, commercial, and/or consumer applications. In particular, crystalline PPS is a high-performance thermoplastic that may be used in the manufacture of a variety of articles in which the mechanical and/or electrical properties of PPS are desired. For example, PPS may be suitable for applications in which high modulus, stiffness, thermal stability, dimensional stability, chemical resistance, flame resistance, and/or electrical non-conductivity are desired. The PPS may be incorporated as a manufacturing component either alone or as a constituent of a thermoplastic blend, i.e., a composition of PPS and one or more other constituents, such as other thermoplastic materials, elastomeric materials, copolymers, resins, reinforcing agents, additives, and so forth.
In particular, use of thermoplastic blends may be advantageous when particular properties of a constituent, such as PPS, are desired though other properties of the constituent may be less desirable. Indeed, due to the wide variety of uses of thermoplastics, the development of suitable thermoplastic blends that accentuate the desired properties of a constituent of the blend while minimizing any undesired properties of the constituent are often desired for particular uses. For example, a PPS-based blend may be desirable as a coating for a flexible substrate, such as a cable or a wire, as a constituent of a fiber, such as may be woven into a cloth or textile product, or as a structural component in the construction of a container for storing volatile liquids. Therefore, it may be desirable to form a thermoplastic blend comprising a suitable grade and/or sufficient quantity of PPS to retain the desired chemical, electrical, thermal, and/or mechanical properties of PPS but also comprising one or more other constituents to impart the desired degree of flexibility and/or impact damage resistance to the blend.
B. Suitable PPS-Based Blends
An example of a PPS-based blend possessing improved flexibility and impact damage resistance compared to PPS and possessing substantial chemical, electrical, and/or flame resistance may be formed by combining a treated PPS resin, an olefinic copolymer, and an elastomer. The PPS-based blend may comprise about 40 to 95% by weight of the treated PPS resin, about 5 to 50% of the olefinic copolymer, and about 1 to 20% by weight of the elastomer. In one embodiment of the PPS-based blend the blend includes less than 10% by weight of the olefinic copolymer. The weight ratio of the olefinic copolymer to the elastomer typically is about 3:1 to about 20:1. As one of ordinary skill in the relevant art will appreciate, the quantities of the blend constituents are selected such that they total 100% by weight of the blend composition.
Prior to combination with the other constituents of the blend, the PPS may be treated to modify reactive end-groups, such as by acidifying the end-groups. In particular, it may be desirable to remove ionic species, such as sodium or chloride ions, associated with the reactive end-groups. This deionization process may be accomplished by a variety of techniques, including treatment of the PPS with acid, hot water, organic solvents, or some combination of these treatments. The deionizing treatments may be performed subsequent to polymerization and recovery of the PPS, such as on the wet PPS fluff or granules. The treatments may be carried out in the presence of heat and/or stirring, if desired, to improve the efficiency of the treatment. As described below, the deionizing treatment may also be accomplished prior to the termination of the PPS polymerization process, i.e., under polymerization conditions. After deionization, the ion content of the treated PPS, such as the sodium ion content, may be less than 900 ppm, if not less than 500 ppm.
The PPS to be treated may include PPS resins having a relatively low molecular weight as well as essentially linear polymers having a relatively high molecular weight. In some instances, such as with low molecular weight resins, the degree of polymerization of the PPS polymers may be increased by heating the PPS polymers in the presence of oxygen or in the presence of a crosslinking agent, such as peroxide, after polymerization. Although PPS prepared by any process may be employed in the present technique, it may be desirable to use a substantially linear polymer having a relatively high molecular weight for forming a PPS blend.
As used herein, PPS comprises at least 70 mole %, and generally 90 mole % or more of recurring units represented by the structural formula:
and may comprise up to 30 mole % of recurring units represented by one or more of the following structural formulas:
To improve the affinity of the PPS resin as described above for the olefinic copolymer, the PPS resin may be subjected to a deionizing treatment, as noted above. In general, the PPS to be treated is in the form of powdery particles, particularly fine particles, to facilitate the efficiency of both the treatment and any subsequent washing processes.
In regard to the acid treatment, the polymerized PPS, including recently polymerized or wet PPS, may be immersed in an acid or acid solution under suitable stirring or heating conditions. For example, an aqueous acetic acid solution with a pH of 4 may be used to treat PPS. The acetic acid solution may be heated to approximately 80° C. to 90° C. and the PPS immersed for approximately 30 minutes under stirring. The treated PPS may then be washed one or more times, such as with distilled or deionized water that may be heated up to 100° C. or higher under pressure. In general, acids which may be employed include those which do not decompose or deteriorate PPS. In addition to acetic acid, other examples of such acids include hydrochloric, sulfuric, phosphoric, silicic, carbonic, and propionic acids.
An organic solvent treatment may be employed instead of or in addition to the acid treatment to improve the affinity of the PPS resin for the olefinic copolymer. Treatment of the PPS by this technique may be accomplished by immersing the PPS in one or more organic solvents, with stirring and/or heat when suitable. The recovered PPS may be treated after washing and drying or while still wet with polymerization solvent or wash water. Indeed, the PPS polymerization mixture may be mixed with an organic solvent or solvents to treat the PPS. Temperature during treatment with the organic solvent may vary, depending on the solvent, from room temperature to approximately 300° C. Sufficient organic solvent treatment, however, can be obtained from approximately 25° C. to 150° C. Depending on the organic solvent and the temperature, the treatment may occur at high pressure to prevent boiling of the solvent. While the period of organic solvent contact is not particularly limited, generally the desired effects may be obtained by treating for approximately five minutes or more, either in a batch or continuous manner. After treatment, the PPS may be washed one or more times with distilled or deionized water, depending on the water solubility and boiling point of the organic solvent. The water wash, if performed, may be carried out at up to 100° C., or higher under pressure.
The organic solvent treatment is not limited in regard to organic solvents to the extent that the organic solvent does not decompose or deteriorate PPS. Examples of organic solvents include, but are not limited to, the nitrogen containing polar solvents (such as N-methylpyrrolidone, N,N-dimethylformamide, N,N-dimethylacetamide, 1,3-dimethylimidazolidinone, hexamethylphosphorylamide, piperadinone group, and so forth). Other possible organic solvents include, sulfoxide and sulfone group solvents (such as dimethyl sulfoxide, dimethyl sulfone, sulfolane, and so forth) and ketone group solvents (such as acetone, methyl ethyl ketone, diethyl ketone, and acetophenone). Additional possible organic solvents include ether group solvents (such as diethyl ether, dipropyl ether, dioxane, and tetrahydrofuran) and halide group solvents (such as chloroform, methylene dichloride, trichloroethylene, ethylene dichloride, perchloroethylene, monochloroethane, dichloroethane, tetrachloroethane, perchloroethane, chlorobenzene, and so forth). Alcohol and phenol group solvents (such as methanol, ethanol, propanol, butanol, pentanol, ethylene glycol, propylene glycol, phenol, cresol, polyethylene glycol, polypropylene glycol, and so forth) and aromatic hydrocarbon group solvents (such as benzene, toluene, xylene, and so forth) may also be employed.
In addition, the PPS may be treated with hot water, such as distilled or deionized water, to improve the affinity of the PPS resin for the olefinic copolymer. Hot water treatment may be performed using water which is 100° C. or higher. Water which is at 170° C. or greater may be more effective at providing the desired chemical modification. For example, a given amount of PPS, including wet or recently polymerized PPS, may be added to a given amount of water, which is then heated, e.g., to 170° C. or higher, and stirred in a pressure vessel. Though the ratio may vary, the ratio of PPS-to-water may generally be 200 g or less of PPS per liter of water. Typically, the water treatment is carried out in an inert atmosphere. After hot water treatment, the PPS may be washed one or more times to remove any undesired components.
While the above treatments may achieve deionization or acidification of the PPS end-groups, in some instances it may be desirable to achieve this process within the reactor under polymerization conditions. In particular, such a treatment may reduce the number of steps, such as wash and recovery steps, associated with PPS production and/or may reduce the ash content, i.e., impurities, in the recovered PPS. Such a process is disclosed in U.S. Pat. No. 5,352,768, which is hereby incorporated by reference.
For example, an acid or acidic solution may be added to the polymerization reaction mixture under polymerization conditions. The acid or acidic solution may be added after an appreciable amount of polymerization has occurred but prior to termination of the polymerization reaction. Typically, the acid or acidic solution is added immediately prior to the termination of the polymerization reaction. A sufficient amount of acid or acidic solution is added to the polymerization mixture to reduce the basicity of the polymerization mixture. In particular, the mole ratio of acid to PPS will be in the range of 0.025:1 to 0.1:1, with a ratio in the range of 0.4:1 to 0.8:1 being typical.
Organic or inorganic acids which are soluble in or miscible with the polar organic compound or solvent, such as N-methyl-2-pyrrolidone, of the polymerization mixture may be used. Examples of suitable organic acids include, but are not limited to, acetic acid, formic acid, oxalic acid, fumaric acid, and monopotassium phthalic acid. Similarly, suitable inorganic acids include hydrochloric acid, monoammonium phosphate, sulfuric acid, phosphoric acid, boric acid, nitric acid, sodium dihydrogen phosphate, ammonium dihydrogen phosphate, carbonic acid, and H2SO.
Subsequent to the addition of the acid or acidic solution, the polymerization may be terminated. Termination may be accomplished by allowing the temperature of the polymerization mixture to fall below that at which substantial polymerization occurs, typically below 235° C. After termination of the polymerization reaction the PPS polymers may be recovered by conventional techniques, i.e., filtration, washing, flash recovery, and so forth. The recovered PPS is effectively deionized by the acid treatment such that the recovered PPS constitutes modified PPS which may be employed in conjunction with the techniques described herein.
For example, a PPS polymer may be prepared by treating the polymerization mixture with acid as follows. First, a mixture of 32.40 kg (71.42 lbs.) of a 50% by weight sodium hydroxide (NaOH) aqueous solution with 39.34 kg (86.74 lbs.) of a solution containing 60% by weight sodium hydrosulfide (NaSH) and 0.4% by weight sodium sulfide (Na2S) may be prepared. This solution, 11.34 kg (25 lbs.) of sodium acetate (NaOAc) powder, and 104.1 L (27.5 gal.) of N-methyl-2-pyrrolidone (NMP) may be added to a stirred (400 rpm) reactor, which may then be purged with nitrogen. This mixture may then be heated to about 172° C. (342° F.) and dehydrated to remove water while the temperature is increased to about 211° C. (411° F.). 63.27 kg (139.49 lbs.) of p-dichlorobenzene (DCB) in 22.7 L (6 gals.) of NMP may be charged to the reactor. The mixture may be heated to about 282° C. (540° F.) and held for 1.5 hours. Then 2,000 mL of glacial acetic acid may be added to the reactor with 3.79 L (1 gal.) of NMP and allowed to react with the reaction mixture for about 5 minutes at 279° C. (535° F.).
The reaction mixture may then be flashed at about 282° C. (540° F.) to remove the NMP and solidify the PPS polymer. The dry, salt-filled polymer may be twice washed with 454.25 L (120 gal.) of deionized water at ambient temperature, then filtered, then washed with 302.83 L (80 gal.) of deionized water at 177° C. (3500 F) for 30 minutes. The solution may be filtered to recover approximately 26.76 kg (59 lbs.) of PPS. The recovered PPS exhibits an ash content of approximately 0.23 or less.
The aforementioned deionization techniques are useful in producing a deionized PPS in which the reactive end-groups have been modified, such as by acidification. However, as one of ordinary skill in the relevant art will appreciate, other deionizing techniques may also be employed which are within the scope of this disclosure. Furthermore, the different deionizing techniques described may be employed separately or in combination. For example, PPS which has been acid treated may subsequently be treated under an organic solvent or with hot water, and so forth.
In addition to deionizing and/or acidifying the PPS, the PPS may also be combined with various additives, such as antioxidants, heat stabilizers, lubricants, nucleating agents, UV stabilizers, carbon black, metal deactivators, plasticizers, titanium dioxide, pigments, clay, mica, flame retardants, processing aids, adhesives, and tackifiers, in amounts which do not affect the desired properties of the PPS or resulting PPS-based blends. Various other polymers may also be present in amounts that do not affect the desired properties. Agents that affect crosslinking, such as peroxides, crosslinking accelerants, and/or crosslinking inhibitors, may also be incorporated into the PPS.
The treated PPS, with or without the additives noted above, may be incorporated into a PPS-based blend. In addition to the treated PPS and any desired additives, the PPS-based blend also comprises an olefinic polymer, such as a copolymer or terpolymer. The olefinic polymer may comprise at least 50% by weight of an α-olefin, such as ethylene, propylene, butene-1, and so forth and less than 50% by weight of a glycidyl ester. Examples of glycidyl esters which may be used in the present technique include glycidyl acrylate, glycidyl methacrylate, glycidyl ethacrylate, and so forth. The olefinic polymer may comprise 40% by weight or less of another copolymerizable unsaturated monomer, such as vinyl ether, vinyl acetate, vinyl propionate, methyl acrylate, methyl methacrylate, acrylonitrile, styrene, and so forth.
In addition to the olefinic copolymer, one or more elastomers may be mixed with the PPS. Typically the elastomer or elastomers comprise at least 50% by weight of ethylene. Possible elastomers include, but are not limited to, the respective copolymers of ethylene/propylene, ethylene/butene, ethylene/propylene/diene, and hydrogenated styrene/butadiene/styrene block. Other possible elastomers include copolymers of ethylene with acrylic acid, methacrylic acid or alkyl esters, and/or the metals salts thereof, and polyamide elastomers. As one of ordinary skill in the art will readily apprehend, other copolymers may also be suitable as an elastomer.
In regard to elastomers comprising copolymers of ethylene with acrylic acid, methacrylic acid, and alkyl esters, and the metal salts thereof, an alkyl group is typically selected which has 1 to 5 carbons atoms. Examples of such elastomers include, but are not limited to, ethylene/acrylic acid ester copolymers, such as the respective copolymers of ethylene/methyl acrylate, ethylene/ethyl acrylate, ethylene/propyl acrylate, and ethylene/butyl acrylate. Similarly, examples of suitable ethylene/methacrylic acid ester copolymers include copolymers of ethylene/methyl methacrylate, ethylene/ethyl methacrylate, ethylene/propyl methacrylate, and ethylene/butyl methacrylate. As noted above, the elastomer may also include or consist of copolymers of ethylene/acrylic acid and/or ethylene methacrylic acid. Likewise, the metal salts of the elastomer copolymers, such as the sodium, zinc, potassium, calcium, lithium, aluminum, and magnesium salts, are intended to be encompassed in the general description of the copolymer, as one of ordinary skill in the art will appreciate.
The selected elastomer or elastomers, along with the olefinic copolymer, acidified PPS, and associated additives may be combined to create the PPS-based blend. As noted above, the PPS-based blend comprises about 40 to 95% by weight of the deionized, i.e., acidified, PPS resin, about 5 to 50% by weight of the olefinic copolymer, and about 1 to 20% by weight of the elastomer. In one embodiment, the blend includes less than 10% by weight of the olefinic copolymer. The weight ratio of the olefinic copolymer to the elastomer typically is about 3:1 to about 20:1. The PPS-based blend may also comprise one or more reinforcing agents, as described below, at 400 parts by weight or less for 100 parts by weight of the total of the PPS, olefinic copolymer, and elastomer. If desired, the reinforcing agents may be treated with a coupling agent, such as silane or titanate, prior to incorporation in the PPS-based blend. Examples of reinforcing agents include fibrous reinforcing agents, such as inorganic and carbonaceous fibers, and hollow or solid granular reinforcing agents, such as silicates, metal oxides, carbonates, sulfates, glass beads, silica, boron nitride, silicon carbide, and so forth.
The PPS-based blend may be melt-blended by a variety of techniques familiar to those of ordinary skill in the art. For example, the PPS, olefinic copolymer, the elastomer, and any desired reinforcing agent or agents may be melt-blended under high shear at a temperature above the melting point of the PPS, such as between 280° to 340° C., in an extruder. The constituents may be pre-mixed or may be metered, simultaneously or separately, into the mixing and blending equipment. The resulting mixture may then be pelletized upon extrusion to facilitate transport and future processing.
The PPS-based blend is generally chemically nonreactive, flame resistant, generally impermeable to liquid and/or vapor, and flexible. The flexibility of the PPS-based blend may be evidenced by the elongation at break associated with the blend, i.e., the elongation of a specimen at the moment of rupture expressed as a percentage of the original length. In particular, the PPS-based blend typically has an elongation at break greater than 150%, as is generally desirable for a flexible coating, such as a wire coating. As one of ordinary skill in the art will appreciate, however, the percentage of elastomer or other constituents may be altered based on the desired embodiment to produce other desired elongation at break ranges. For example, a PPS-based blend with an elongation to break between 100% to 150% may be produced using a lower percentage of elastomer. Similarly, a PPS-based blend with an elongation to break between 150% to 200% or greater may be produced using a higher percentage of elastomer.
C. Applications of a Flexible and/or Impact Resistant PPS-Based Blend
1. Coatings for Flexible Substrates
The pelletized PPS-based blend may be used in the construction of commercial or manufactured goods, either as the sole material of construction or as a constituent of a composite construction material. For example, the PPS-based blend may be used as a coating 22 for wires 24 or other flexible media, as depicted in
While wires 24 and cables are examples of flexible media which may be coated by the PPS-based blend, other flexible substrates may be similarly coated. For example, a coating comprising a PPS-based blend may be applied to the interior or exterior surfaces of an article, such as a gas tank, chemical drum, kitchen utensil, and so forth. Such surfaces may be inherently flexible due to their composition, and may benefit from a coating of a flexible PPS-based blend. The coating may act as a protective sheathing of the underlying substrate, such as by providing mechanical, chemical, thermal, or electrical protection, while possessing some degree of impact resistance.
Though coatings of other substrates is one possible application of the PPS-based blend, the PPS-based blend itself may be the primary material of construction. For example, single-piece or multi-piece containers or articles may be formed which are chemically non-reactive and/or flame resistant and which possess some degree of flexibility. To construct these articles, the PPS-based blend may be molded or formed by a variety of known techniques, including, but not limited to injection molding, extrusion molding, compression molding, transfer molding, and blow forming.
2. Fibers
The PPS-based blend may also, either alone or in conjunction with other constituents, be formed as strands or fibers. The PPS-blend fibers may in turn be woven into cloth or fabric that may be used to form filters, canvas, clothing, and insulation, such as electrical insulation. For example, the PPS-based blend may be extruded or formed as threads or strands which may comprise the fibers themselves or which may be associated lengthwise, i.e., longitudinally, to form the fibers. Once formed, the PPS-blend fibers may be woven to form a textile, fabric, or cloth, or otherwise associated, such as to form filter material or insulation. Because the fibers are formed from the PPS-based blend, the fibers, and materials made from the fibers, possess greater flexibility and less brittleness relative to pure PPS. The flexibility of the fibers may also depend on the length of PPS polymers comprising the fibers or strands.
3. Multi-Layer Structures
Alternatively, the PPS-blend may be incorporated as one or more layers of a multi-layer structure that possesses additional desired properties or different properties on the exposed surfaces. For example, referring to
The multi-layer structure 50 may include additional layers that impart impact resistance and/or formability to the multi-layer structure 50. For example, an outer layer 54 may serve as a protective coating. The outer layer 54 also may provide desired structural and/or mechanical properties. The outer layer 54 may be composed of PPS, PPS-based blends, polyethylene (PE), high-density polyethylene (HDPE), polypropylene (PP), nylon, poly(butylene terephthalate) (PBT), poly(ethylene terephthalate) (PET) or other polymers having the desired properties. The outer layer 54 may also comprise a blend of polymers, or it may include a recycled polymer, such as recycled HDPE, that possesses the desired properties.
In addition, as depicted in
Based upon the compositions of the barrier layer 52, outer layer 54, and secondary layer 56 (if present), one or more tie layers 58 may be present in the multi-layer structure 50 to facilitate the adhesion of one layer to another. For example, materials such as Xtel® XE3200 (a PPS-based blend available from Chevron Phillips Chemical Company LP) and/or linear low-density polyethylene (LDPE) may be used in the construction of tie layers 58. The composition of a tie layer 58 may be determined by the properties of the adjacent layers, such as the dimensional stability of an adjacent layer over the range of temperatures in the expected environment. For example, a tie layer 58 composed of Xtel® XE3200 may be desirable adjacent a barrier layer 52 composed of PPS or a PPS-based blend. Similarly, a tie layer 58 composed of linear LDPE may be desirable adjacent an outer layer 54 or secondary layer 56 of HDPE or recycled HDPE. If desired, multiple tie layers 58 may be used, as depicted, to accommodate the different compositions of the adjacent layers. In such circumstances, the tie layers 58 may be adhered together along one facing to accomplish the bonding of otherwise dissimilar interior and exterior layers.
The multi-layer structure 50 may be created in a variety of ways in addition to or instead of the incorporation of tie layers 58. For example, the barrier layer 52, outer layer 54, and any additional layers may be subjected to heat and pressure, i.e., lamination, to bond two or more of the layers together. Alternatively the layer surfaces or adhesives disposed between the layers may be activated by an energy source, such as UV, IR, thermal, or plasma, thereby bonding the layers together. As another alternative, a layer of the multi-layer structure 50 may be applied as a laminated film, deposited via spray or plasma spray, or deposited via the evaporation of a solvent to leave a residual layer of solute.
While the aforementioned techniques assume the construction of a multi-layer structure 50 from two or more separate sheets or films composed of the desired polymer or polymer blend, the multi-layer structure 50 may instead be created by a coextrusion or by a multi-layer extrusion process. For example, the multi-layer structure 50 may be constructed by a standard blow molding process, using extrusion, or by injection molding by which layers are sequentially deposited. However, as one of ordinary skill in the art will appreciate, the aforementioned processes are not mutually exclusive and a combination of processes may be utilized in constructing the overall multi-layer structure 50.
a. Creating Components or Articles Using Multi-Layer Structures
Once constructed, the multi-layer structure 50 may be formed, by shaping or molding, into one or more articles or components of interest. Such articles may include containers, such as those used to store and/or transport fuel, chemicals, or beverages, in which the chemical inertness, impermeability, and/or flammability resistance of the interior barrier layer is desirable. For example, a single-piece construction article 80 comprising the multi-layer structure 50 may be constructed using blow molding, as depicted in
Referring to
While this is one manner in which a single-piece article 80 may be formed from a multi-layer structure 50, in many contexts it may be desirable to construct a multi-piece article 100 from a multi-layer structure 50. For example, it may be desirable to construct fuel or chemical tanks that contain interior components or that are prohibitively large for single piece construction techniques. In these instances, the multi-layer structure 50 may be formed into the desired components, such as body components, fuel filler necks, and so forth, which may be subsequently assembled into the desired multi-piece article 100.
For example, individual components of a multi-piece article 100 may be created by a blow forming process, a variation on the blow molding process depicted in
Alternatively, a multi-layer structure 50 may be formed into a container half 102, 103 or other piece of the multi-piece article 100 by other forming processes, such as vacuum forming, as depicted in
A component of a multi-piece article 100, such as the container half 102, 103, may be formed by other methods as well. For example, the multi-layer structure 50 may be constructed during the forming process, such as in an injection compression molding process. To construct the multi-layer structure 50 in conjunction with forming, the barrier layer 52 may first be inserted, deposited, or applied to the mold as a film, a sheet, a coating of particles, and so forth. The next layer, such as a secondary layer 56, a tie layer, or an outer layer 54, may be applied over the barrier layer 54 via injection compression molding. The heat and pressure of the injection molding process promotes adhesion of the various layers. Additional layers may be similarly applied until the desired component, comprising the multi layer structure 50, is constructed. Once the components of the multi-piece article are formed, assembly of the multi-piece article 100 may proceed as described above, including inclusion of any desired internal components 104. While the forming of components has been described via blow forming, vacuum forming, and injection compression molding, one of ordinary skill in the art will readily apprehend that other forming techniques, such as pressure forming and cold forming, may also be used to form components of a multi-piece article 100.
b. Assembling Multi-Piece Articles
The various components of a multi-piece article 100 may be assembled by a variety of techniques including, but not limited to, hot plate welding, IR or UV activated surfaces or adhesives, EMA bonding, and hot air welding. For example, as depicted in
As depicted in
While the multi-piece article 100 has been depicted in the present discussion as a two-piece container for simplicity, one of ordinary skill in the art will readily apprehend that the technique may be readily adapted to articles 100 possessing more pieces or more complex pieces. Indeed, the economics of tooling and the build volumes will typically determine the number of components of a multi-piece article 100, and the present technique may be readily adapted for use with more complex multi-piece articles 100. For example, fuel tanks 130 may be formed and incorporated into motor vehicles 132, such as cars, trucks, motorcycles, boats, aircraft, and so forth, as depicted in
Though the preceding discussion focuses primarily on the possibility of using multi-layer structures comprising one or more layers of PPS or PPS-based layers to form either single- or multi-piece articles, a single layer of PPS may be similarly employed. For example, a container or fuel tank may be constructed of a single layer of PPS or a multi-layer structure in which the assorted layers are PPS or PPS-based blends. Such a container or fuel tank would have the impermeability characteristics as described above if constructed in accordance with the above techniques, i.e., forming an impermeable weld or junction 118 of PPS or PPS-based blends. The respective PPS components may be formed by the techniques described above, such as blow-forming, vacuum forming, and so forth and may be assembled by the disclosed techniques, such as hot plate welding or hot air welding.
While the invention may be susceptible to various modifications and alternative forms, specific embodiments have been shown by way of example in the drawings and will be described in detail herein. However, it should be understood that the invention is not intended to be limited to the particular forms disclosed. Rather, the invention is to cover all modifications, equivalents and alternatives falling within the spirit and scope of the invention as defined by the following appended claims.
This application claims priority to provisional application 60/496,097, filed on Aug. 18, 2003.
Number | Date | Country | |
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60496097 | Aug 2003 | US |