阅读说明：本技术 抗冲击改性的聚(亚芳基硫醚)组合物 (Impact-modified poly (arylene sulfide) compositions ) 是由 W.E.萨特奇 于 2018-11-30 设计创作，主要内容包括：抗冲击改性的聚(亚芳基硫醚)组合物披露了制造聚合物组合物的方法,该方法包括：(i)使聚(亚芳基硫醚)(PAS)与包含锌离子的水溶液接触,优选在聚合后回收该PAS期间,以及ii)使该PAS与乙烯共聚物抗冲击改性剂接触。还描述了由该方法制造的聚合物组合物,以及包含该聚合物组合物的成型制品。(Impact modified poly (arylene sulfide) compositions disclose a method of making a polymer composition comprising: (i) contacting a poly (arylene sulfide) (PAS) with an aqueous solution comprising zinc ions, preferably during the recovery of the PAS after polymerization, and ii) contacting the PAS with an ethylene copolymer impact modifier. Also described are polymer compositions made by the method, and shaped articles comprising the polymer compositions.)

1. A method of making a polymer composition, the method comprising:

(i) contacting a poly (arylene sulfide) (PAS) with an aqueous solution comprising zinc ions,

wherein the contacting increases the zinc content of the poly (arylene sulfide) (PAS) to at least 1000ppm as measured by inductively coupled plasma optical emission spectroscopy (ICP-OES); and

(ii) contacting the poly (arylene sulfide) (PAS) with an ethylene copolymer impact modifier.

2. The process of claim 1, wherein the melt crystallization temperature (Tmc) of the poly (arylene sulfide) (PAS) is at least 225 ℃ as measured by Differential Scanning Calorimetry (DSC) according to ASTM D3418 after contacting with the aqueous solution comprising zinc ions.

3. The method of any one of claims 1 and 2, wherein contacting the poly (arylene sulfide) (PAS) with the aqueous solution comprising zinc ions comprises washing particles of the poly (arylene sulfide) (PAS) with the aqueous solution comprising zinc ions during recovery of the poly (arylene sulfide) (PAS) after polymerization.

4. The method of claim 3, wherein washing the particles of poly (arylene sulfide) (PAS) comprises removing alkali metal halides.

5. The process of any one of claims 1 to 4, wherein the aqueous solution comprising zinc ions comprises dissolved zinc acetate.

6. The method of any one of claims 1 to 5, wherein the poly (arylene sulfide) (PAS) is selected from the group consisting of: poly (2, 4-toluene sulfide), poly (4,4' -biphenylene sulfide), poly (p-phenylene sulfide) (PPS), poly (o-phenylene sulfide), poly (m-phenylene sulfide), poly (xylene sulfide), poly (ethylisopropylene phenylene sulfide), poly (tetramethylphenylene sulfide), poly (butylcyclohexylphenylene sulfide), poly (hexyldodecylphenylene sulfide), poly (octadecylphenylene sulfide), poly (phenylene sulfide), poly- (tolylene sulfide), poly (benzylphenylene sulfide), poly [ octyl-4- (3-methylcyclopentyl) phenylene sulfide ], or a combination thereof.

7. The method of any one of claims 1 to 6, wherein the poly (arylene sulfide) (PAS) is a poly (arylene sulfide) (PAS) comprising at least 50 mol% of recurring units (R) of formula (A)_PPS) Poly (p-phenylene sulfide) (PPS):

8. the process of any one of claims 1 to 7, wherein the ethylene copolymer impact modifier comprises at least 50 wt.%, preferably at least 60 wt.% ethylene repeating units and 50 wt.% or less, preferably 40 wt.% or less of (meth) acrylate group-containing repeating units.

9. The method of any one of claims 1 to 8, wherein the ethylene copolymer impact modifier comprises ethylene/acrylate/glycidyl methacrylate, ethylene/ethylene butyl acrylate, ethylene/ethylene acrylate, ethylene/methyl acrylate, or a combination thereof.

10. The method of any one of claims 1 to 9, wherein the polymer composition further comprises a reinforcing filler, preferably glass fibers.

11. A polymer composition made by the method of any one of claims 1 to 10.

12. The polymer composition of claim 11, wherein the polymer composition exhibits at least 10kJ/m as measured according to ISO 180/a²Notched izod impact resistance.

13. The polymer composition of any one of claims 11 and 12, wherein the zinc ion is bonded to the PAS poly (arylene sulfide) (PAS).

14. A shaped article comprising a polymer composition produced by the method of any one of claims 1 to 10.

15. A process for the manufacture of a shaped article comprising injection molding or 3D printing a polymer composition manufactured by the process of any one of claims 1 to 10.

Technical Field

The present application relates to a method of making a polymer composition, the method comprising: (i) contacting a poly (arylene sulfide) (PAS) with an aqueous solution comprising zinc ions, preferably during the recovery of the PAS after polymerization, and ii) contacting the PAS with an ethylene copolymer impact modifier. Also described are polymer compositions made by the method, and shaped articles comprising the polymer compositions.

Background

Poly (arylene sulfide) (PAS) is a high temperature semi-crystalline engineering polymer with excellent chemical resistance, high heat deflection temperature, good electrical insulation properties, and inherent flame retardancy.

PAS are often injection molded into components for various applications, such as automotive under-the-hood applications and electrical applications. Injection molding cycle times are highly dependent on the crystallization kinetics of the injected material, with faster crystallization kinetics leading to faster cycle times and increased production rates. Thus, higher production rates of injection molded components can be achieved using PAS compositions having a high melt crystallization temperature (Tmc) (i.e., Tmc ≧ 225 ℃ as measured by Differential Scanning Calorimetry (DSC) in accordance with ASTM D3418) than using PAS compositions having a lower Tmc.

Formulations comprising acetic acid washed PAS may exhibit high Tmc, and thus faster crystallization kinetics, compared to water washed PAS formulations. However, when the composition comprises an ethylene copolymer impact modifier, no high Tmc is observed in the acetic acid washed PAS composition.

Accordingly, there is a need for impact modified PAS compositions that also exhibit faster crystallization kinetics.

Detailed Description

Described herein is a method of making a polymer composition, the method comprising: (i) contacting PAS with an aqueous solution comprising zinc ions to increase the zinc content of the PAS to at least 1000ppm as measured by inductively coupled plasma optical emission spectroscopy (ICP-OES), and ii) contacting the PAS with an ethylene copolymer impact modifier. Also described are polymer compositions made by the method, and shaped articles comprising the polymer compositions.

The conventional process for manufacturing PAS results in PAS having a zinc content of less than 1000ppm as measured by ICP-OES. Applicants have unexpectedly found that significantly improved crystallization kinetics are achieved in a PAS composition comprising an ethylene copolymer impact modifier when the PAS is contacted with an aqueous solution comprising zinc ions such that the zinc content of the PAS is increased to at least 1000ppm as measured by ICP-OES as described in the examples below. After contacting, the zinc content of PAS is preferably increased to at least 1100ppm, 1200ppm, 1300ppm, 1400ppm, 1500ppm, and most preferably at least 1600 ppm. All zinc contents described herein were measured by ICP-OES as described in the examples. Preferably, all of the zinc content of the PAS, more preferably all of the zinc content of the polymer composition, and most preferably both, are derived from zinc ions in an aqueous solution.

The aqueous solution containing zinc ions may be any aqueous based solution containing free zinc cations having the ability to form ionic bonds with the end groups of PAS by ion exchange. The aqueous solution containing zinc ions may further contain a cation or an anion other than zinc ions. Preferably, the aqueous solution containing zinc ions is a solution of zinc acetate in water, although other water soluble zinc containing salts may also be used. The concentration of zinc ions in the aqueous solution comprising zinc ions should be sufficient to increase the zinc content of PAS to at least 1100ppm, 1200ppm, 1300ppm, 1400ppm, 1500ppm, and most preferably at least 1600 ppm. In some embodiments, the concentration of zinc ions in the aqueous solution is at least 0.01M.

Preferably, the PAS is contacted with the aqueous solution comprising zinc ions prior to the polymer composition comprising PAS (e.g., prior to contacting the PAS with the ethylene copolymer impact modifier or other ingredients in the polymer composition).

Methods of PAS production, particularly poly (p-phenylene sulfide) (PPS) production, are known in the art and are described in detail, for example, in U.S. Pat. nos. 3,919,177, 3,354,129, 4,038,261, 4,038,262, 4,038,263, 4,064,114, 4,116,947, 4,282,347, 4,350,810, and 4,808,694, each of which is incorporated herein by reference in its entirety. General conditions for producing PAS (e.g., PPS) are described, for example, in U.S. patent nos. 5,023,315, 5,245,000, 5,438,115, and 5,929,203, each of which is incorporated herein by reference in its entirety.

In some embodiments, contacting the PAS with the aqueous solution containing zinc ions may be incorporated into the PPS recovery stage after polymerization. Generally, a PAS production process includes a polymerization stage in which PAS is synthesized by contacting at least one halogenated aromatic compound having two halogens, a sulfur compound, and a polar organic compound to form a precipitate of PAS in a reaction mixture slurry. Subsequently, during the recovery stage, the synthesized PAS particles (e.g., PPS particles) are recovered from the reaction mixture slurry and purified by any method capable of separating and purifying solid particulates from liquids. PAS production processes can form alkali metal halide byproducts. The by-product alkali metal halide may be removed and the PAS purified during the recovery stage of PAS (e.g., PPS).

In some embodiments, during a recovery stage of a process for producing PAS, the PAS is contacted with an aqueous solution comprising zinc ions. For example, an aqueous solution containing zinc ions may be used as the aqueous solution one or more times during the recovery stage described below.

The recovery stage may comprise one or more steps during which the PAS is contacted with an aqueous solution (e.g. washed with an aqueous solution), as described below. For example, a procedure that may be utilized to recover PAS particles from a reaction mixture slurry may include: i) filtering; ii) washing the PAS with a liquid (e.g., water or an aqueous solution); or iii) after filtering and washing the PAS with a liquid (e.g., water or an aqueous solution), diluting the reaction mixture with a liquid (e.g., water or an aqueous solution). For example, the reaction mixture slurry may be filtered to recover PAS (e.g., PPS) particles, which may be slurried in a liquid (e.g., water or an aqueous solution) and subsequently filtered to remove alkali metal halide by-products (and/or other liquids, e.g., water, soluble impurities). In general, the step of slurrying PAS with a liquid after filtering and recovering PAS may occur multiple times (if necessary) to obtain a desired level of purity of PAS, and the PAS may be washed with one or more aqueous solutions.

The one or more aqueous solutions described in the previous paragraph can be an aqueous solution comprising zinc ions.

In some embodiments, the aqueous solution comprising zinc ions is a washing solution, and the PAS is contacted with the aqueous solution comprising zinc ions in one or more steps during a recovery stage of the PAS as described above. The PAS may be contacted (e.g., washed) with the aqueous solution containing zinc ions once, twice, three times, or more. Preferably, the PAS is contacted (e.g., washed) more than once with the aqueous solution comprising zinc ions. The PAS is contacted with the aqueous solution comprising zinc ions a sufficient number of times or for a sufficient total time to increase the zinc content of the PAS to at least 1000ppm, 1100ppm, 1200ppm, 1300ppm, 1400ppm, 1500ppm, and most preferably at least 1600ppm at the end of the recovery stage.

In some embodiments, contacting the PAS with an aqueous solution comprising zinc ions (e.g., washing the PAS with an aqueous solution comprising zinc ions as described herein) increases the zinc content of the PAS and decreases the concentration of alkali metal halide byproducts (e.g., separates the alkali metal halide byproducts from the PAS).

The melt crystallization temperature (Tmc) of PAS is preferably at least 225 ℃ after contacting with the aqueous solution comprising zinc ions. In some embodiments, the Tmc of the PAS is at least 226 ℃. In some embodiments, the Tmc of the PAS is at least 229 ℃. When PAS is included in the polymer composition (e.g., after contacting the PAS with the ethylene copolymer impact modifier or other ingredients in the polymer composition), the Tmc of the PAS is preferably at least 225 ℃, preferably at least 226 ℃. In some embodiments, when PAS is included in the polymer composition, the Tmc of PAS is at least 229 ℃. Tmc was measured by Differential Scanning Calorimetry (DSC) according to ASTM D3418, as described in the examples below.

It has been surprisingly found that the high Tmc exhibited by PAS after contacting with (e.g., washing with) the aqueous solution comprising zinc ions described herein imparts improved crystallization kinetics to a polymer composition comprising PAS and an ethylene copolymer impact modifier. The improved crystallization kinetics of the polymer compositions of the present invention allow for faster injection molding cycle times and associated increased production rates.

The polymer composition may be manufactured by methods well known to those skilled in the art. For example, such methods include, but are not limited to, melt mixing methods. Melt mixing processes are typically carried out by heating the polymer components above the melting temperature of the thermoplastic polymers, thereby forming a melt of these thermoplastic polymers. Suitable melt-mixing devices are, for example, kneaders, Banbury mixers, single-screw extruders and twin-screw extruders. Preferably, an extruder is used which is equipped with means for feeding all the desired components into the extruder (into the throat of the extruder or into the melt). In a process for preparing a polymer composition, the components of the polymer composition (e.g., PAS, ethylene copolymer impact modifier, optional reinforcing filler, and optional additives) are fed to and melt mixed in a melt mixing device. The components may be fed simultaneously or may be fed separately in the form of a powder mixture or a mixture of granules (also referred to as a dry blend).

The order of combination of the components during melt mixing is not particularly limited. In one embodiment, the components may be mixed in a single batch such that the desired amounts of the components are added together and then mixed. In other embodiments, the first subset of components may be initially mixed together and one or more of the remaining components may be added to the mixture for further mixing. For clarity, the desired total amounts of the components do not have to be combined as separate amounts. For example, for one or more of the components, a portion of the amount may be initially added and mixed, and then some or all of the remainder may be added and mixed.

Poly (arylene sulfide) (PAS)

As used herein, "poly (arylene sulfide) (PAS)" means that 50 mol% of its recurring units are of the formula(R) repeating unit of- (Ar-S) -_PAS) Wherein Ar is an aromatic group. Preferably, at least 70 mol%, 80 mol%, 90 mol%, 95 mol%, 99 mol% of the repeating units in the PAS are repeating units (R) having the formula- (Ar-S) -_PAS). For clarity, as used herein, mole percentages are relative to the total number of repeat units in the polymer, unless explicitly indicated otherwise.

As used herein, "poly (p-phenylene sulfide) (PPS)" means that at least 50 mol% of its repeating units are repeating units (R) having formula (A)_PPS) Any polymer of (a):

preferably, at least 70 mol%, 80 mol%, 90 mol%, 95 mol%, 99 mol% of the recurring units in the PPS are recurring units having the formula A (R)_PPS)。

In some embodiments, the PAS comprises poly (2, 4-toluene sulfide), poly (4,4' -biphenylene sulfide), poly (p-phenylene sulfide) (PPS), poly (o-phenylene sulfide), poly (m-phenylene sulfide), poly (xylene sulfide), poly (ethylisopropylene phenylene sulfide), poly (tetramethylphenylene sulfide), poly (butylcyclohexylphenylene sulfide), poly (hexyldodecylphenylene sulfide), poly (octadecylphenylene sulfide), poly (phenylene sulfide), poly (tolylene sulfide), poly- (tolylene sulfide), poly (benzylphenylene sulfide), poly [ octyl-4- (3-methylcyclopentyl) phenylene sulfide ], or a combination thereof. Preferably, the PAS is poly (p-phenylene sulfide) (PPS).

PPS is available from Solvay Specialty Polymers USA (Solvay Specialty Polymers USA, &lTtT transfer = L "&gTt L &lTt/T &gTt. L. C) under the trade nameManufactured and sold.

Any amounts stated herein in weight percent are relative to the total weight of the polymer composition, unless otherwise indicated. Preferably, the polymer composition comprises more than 50 wt.%, preferably at least 60 wt.% PAS (e.g. PPS). Additionally or alternatively, in some embodiments, the PAS polymer includes no more than 90 wt.%, preferably no more than 80 wt.% PAS. In some embodiments, the amount of PAS in the polymer composition ranges from 60 wt.% to 90 wt.%, preferably from 60 wt.% to 80 wt.%.

In some embodiments, the amount of PAS in the polymer composition that has been contacted with the aqueous solution comprising zinc ions as described herein is at least 50 wt.%, preferably at least 60 wt.%, 70 wt.%, 80 wt.%, 90 wt.%, and most preferably at least 99 wt.%, based on the total weight of PAS in the polymer composition.

Ethylene copolymer impact modifiers

The polymer composition includes an ethylene copolymer impact modifier. As used herein, "copolymer" means a polymer containing two or more different repeat units, and includes terpolymers. The ethylene copolymer impact modifier comprises at least 50 wt.%, preferably at least 55 wt.%, preferably at least 60 wt.% of ethylene repeating units.

Preferably, the ethylene copolymer impact modifier comprises 50 wt.% or less, preferably 45 wt.% or less, preferably 40 wt.% or less of repeating units comprising a (meth) acrylate group.

In some embodiments, the ethylene copolymer impact modifier comprises (i) at least 50 wt.% ethylene, (ii)0 to 50 wt.% of a C1-C12 alkyl (meth) acrylate or vinyl ether, and (iii)0 to 50 wt.% of an unsaturated C4-C11 epoxide, preferably glycidyl acrylate, Glycidyl Methacrylate (GMA), allyl glycidyl ether, vinyl glycidyl ether, or glycidyl itaconate, or an unsaturated C2-C11 isocyanate, preferably vinyl isocyanate or isocyanoethyl methacrylate.

In some embodiments, the ethylene copolymer impact modifier comprises (i) at least 55 wt.%, preferably at least 60 wt.% ethylene, (ii)0.5 to 35 wt.% of a C1-C12 alkyl (meth) acrylate, preferably methyl acrylate, isobutyl acrylate, or n-butyl acrylate, and (iii)0.5 to 10 wt.% of an unsaturated C4-C11 epoxide, preferably glycidyl methacrylate or glycidyl acrylate.

In an alternative embodiment, the ethylene copolymer impact modifier comprises (i) at least 50 wt.%, preferably at least 60 wt.% ethylene, and (ii) less than 50 wt.%, preferably less than 40 wt.% of a C1-C12 alkyl (meth) acrylate, preferably methyl acrylate, isobutyl acrylate, or n-butyl acrylate.

Most preferred ethylene copolymer impact modifiers are those selected from the group consisting of: ethylene/acrylate/glycidyl methacrylate, ethylene/ethylene butyl acrylate, ethylene/ethylene acrylate, ethylene/methyl acrylate, and combinations thereof.

In some embodiments, the impact modifier is a random copolymer of ethylene and glycidyl methacrylate, and/or a random terpolymer of ethylene, methyl acrylate, and glycidyl methacrylate. Examples of such copolymers include those available from Arkema, inc (Arkema), respectivelyAX8840 andAX 8900。

in some embodiments, the ethylene copolymer impact modifier is a random copolymer of ethylene and ethylene butyl acrylate, ethylene and ethylene acrylate, or ethylene and methyl acrylate. Examples of such copolymers are available from DuPont corporation (Dupont)An AS copolymer.

In some embodiments, the ethylene copolymer impact modifier is an ionomer of an ethylene acid acrylate terpolymer, preferably a zinc ionomer of an ethylene acid acrylate terpolymer. Such terpolymers are available from Dupont asAre available.

The polymer composition may include one, two or more ethylene copolymer impact modifiers.

In some embodiments, the ethylene copolymer impact modifier is 0.5 wt.% to 30 wt.%, preferably 1 wt.% to 25 wt.%, preferably 1 wt.% to 20 wt.%, 1 wt.% to 15 wt.%, 1 wt.% to 10 wt.%, 1 wt.% to 7 wt.%, 1 wt.% to 6 wt.%, 5 wt.% to 6 wt.%, based on the total weight of the polymer composition.

In some embodiments, the polymer composition has at least 10kJ/m as measured according to ISO 180/A²Notched izod impact resistance.

Optional reinforcing fillers

The polymer composition may optionally comprise reinforcing fillers, such as fibrous fillers or particulate fillers. A fiber reinforced filler is a material having a length, a width, and a thickness, wherein the average length is significantly greater than both the width and the thickness. Preferably, such materials have an aspect ratio (defined as the average ratio between length and the smallest of width and thickness) of at least 5. Preferably, the aspect ratio of these reinforcing fibers is at least 10, more preferably at least 20, still more preferably at least 50. These particulate fillers have an aspect ratio of at most 5, preferably at most 2.

Preferably, the reinforcing filler is selected from mineral fillers such as talc, mica, kaolin, calcium carbonate, calcium silicate, magnesium carbonate, boron nitride; glass fibers; carbon fibers, boron carbide fibers; wollastonite; silicon carbide fibers; boron fibers, graphene, Carbon Nanotubes (CNTs), and the like. Most preferably, the reinforcing filler is glass fibers, preferably chopped glass fibers, or carbon fibers, preferably chopped carbon fibers.

The amount of reinforcing filler may range from 1 to 40 wt.%, preferably from 5 to 35 wt.% and most preferably from 10 to 30 wt.% in the case of particulate filler, and from 5 to 50 wt.%, preferably from 10 to 40 wt.% and most preferably from 15 to 30 wt.% in the case of fibrous filler, based on the total weight of the polymer composition. Preferably, the polymer composition comprises from 20 to 60 wt.%, preferably from 20 to 50 wt.%, 25 to 35 wt.%, most preferably about 30 wt.% of glass or carbon fibers, most preferably glass fibers. In some embodiments, the polymer composition is free of fibrous fillers, particulate fillers, or both.

Optional additives

The polymer composition may further comprise optional additives such as titanium dioxide, ultraviolet light stabilizers, heat stabilizers, antioxidants (such as organic phosphites and phosphonites), acid scavengers, processing aids, nucleating agents, lubricants, flame retardants, smoke suppressants, antistatic agents, antiblock agents, and conductive additives (such as carbon black).

When one or more optional additives are present, their total concentration is preferably less than 10 wt.%, more preferably less than 5 wt.%, and most preferably less than 2 wt.%.

Molded article and method of manufacture

Exemplary embodiments also include shaped articles comprising the polymer compositions and methods of making these shaped articles.

The polymer composition can be well suited for making articles useful in a wide variety of applications. These shaped articles can be made from the polymer composition using any suitable melt processing method, such as injection molding, extrusion molding, rotational molding, or blow molding; however, the crystallization kinetics and toughness of the polymer composition make it particularly suitable for use in injection molded parts, such as automotive under-the-hood and chassis parts (e.g., hydraulic pump assemblies, overmolded sensors, electric motor assemblies) and piping assemblies (e.g., piping pump valves, manifolds, and gauges).

Exemplary embodiments are also directed to methods of making a shaped article by additive manufacturing, wherein the shaped article is printed from a polymer composition. These methods include printing a layer of a shaped article from a polymer composition, as described below.

An additive manufacturing system (e.g., a 3D printing system) is used to print or otherwise build a shaped object from a digital representation of the shaped object by one or more additive manufacturing techniques. Examples of commercially available additive manufacturing techniques include extrusion-based techniques, selective laser sintering, powder/binder jetting, electron beam melting, and stereolithography processes. For each of these techniques, the digital representation of the shaped object is initially cut into a plurality of horizontal layers. For each layer, a tool path is then generated that provides instructions for a particular additive manufacturing system to print a given layer.

Thus, some examples include a method of manufacturing a shaped article, the method comprising printing a layer of a polymer composition to form the shaped article by an extrusion-based additive manufacturing system (e.g., FFF), a powder-based additive manufacturing system (e.g., S L S), or a continuous Fiber Reinforced Thermoplastic (FRTP) printing method.

Exemplary embodiments will now be further illustrated in the following non-limiting examples.

Examples of the invention

The various polymer compositions were evaluated for tensile properties, impact strength, and melt crystallization temperature (Tmc).

Material

PPS

PPS QA250N (acetic acid washed), available from Suweiter polymers, Inc., USA, has a melt flow rate of 430g/10min as evaluated by ASTM D1238B at 316 ℃ with a weight (MFR) of 5 kg.

PPS (deionized water washed), MFR 140g/10 min.

PPS (zinc acetate washed), MFR 136g/10 min.

PPS (KOH washed), MFR 160g/10 min.

PPS QC220N (calcium acetate washed), MFR 175g/10 min.

Ethylene copolymer impact modifiers

AX8840, random copolymer of ethylene and glycidyl methacrylate (8 wt.%) available from arkema.

AX8900, a random terpolymer of ethylene, methyl acrylate (24 wt.%), and glycidyl methacrylate (8 wt.%) available from arkema.

AS, ethylene/butyl acrylate/glycidyl methacrylate terpolymer available from dupont.

9320W, zinc ionomer (partially neutralized zinc salt) of ethylene acid acrylate terpolymer available from DuPont.

Antioxidant agent

1010 available from BASF corporation (BASF).

Organofunctional silanes

Silane Silquest A-1524, available from Momentive Performance materials, Inc., of advanced materials, McTown.

Silane Silquest A-187, available from the Mitigo high New materials group.

High Density Polyethylene (HDPE)

6007 supplied by Chevron Phillips chemical company

Preparation of deionized water washed PPS

Deionized water washed PPS was synthesized and recovered from the reaction mixture according to the methods described in U.S. Pat. nos. 3,919,177 and 4,415,729, and washed twice with deionized water at 60 ℃ for at least 5 minutes.

Preparation of Zinc acetate washed PPS

The zinc acetate washed PPS was synthesized and recovered from the reaction mixture according to the methods described in U.S. Pat. nos. 3,919,177 and 4,415,729, washed twice with deionized water at 60 ℃ for at least 5 minutes, then washed once with 0.01 mol/L aqueous zinc acetate solution at 60 ℃ for at least 5 minutes, and then washed once more with deionized water at 60 ℃ for at least 5 minutes.

Preparation of potassium hydroxide washed PPS

Potassium hydroxide washed PPS was synthesized and recovered from the reaction mixture according to the methods described in U.S. Pat. nos. 3,919,177 and 4,415,729, washed twice with deionized water at 60 ℃ for at least 5 minutes, then washed once with 0.02 mol/L aqueous potassium hydroxide solution at 60 ℃ for at least 5 minutes, and then washed once more with deionized water at 60 ℃ for at least 5 minutes.

Mixing and blending

Use ofThe compositions shown in tables 1, 2 and 3 below were compounded at 200rpm and 16-18kg/h using a ZSK-26 co-rotating twin screw extruder (having an L/D ratio of 48: 1.) barrel temperature set point of 305 ℃ and die temperature set point of 300 ℃.

Evaluation of thermal and mechanical Properties

The melt flow rate of the PPS polymer was determined according to ASTM D1238B at 316 ℃ with a 5kg weight.

The zinc content of the PPS polymer is determined by inductively coupled plasma optical emission spectroscopy (ICP-OES) analysis of dilute acid solutions of the combustion residues of the polymer. For each sample, approximately 1g was weighed on an analytical balance into a platinum crucible and then ashed overnight in a laboratory furnace. The sample crucible was placed on a hot plate and any residue was leached with dilute hydrochloric acid for about 30min at a hot plate setting of about 260 ℃. After cooling, the contents of each crucible were quantitatively transferred to a25 ml volumetric flask and made up with deionized water. The sample extracts were then analyzed by ICP-OES (Perkin Elmer Optima 8300) using a Semi-Quantitative Metal assay (Semi-Quantitative Metal surface method).

The melt crystallization temperature (Tmc) of the PPS polymer in the composition was determined by differential scanning calorimetry according to ASTM D3418 with heating at 20 ℃/min to 350 ℃ and then cooling at 20 ℃/min.

Test specimens are injection molded from the composition according to ISO 294 at a melting temperature of 300 ℃ to 350 ℃ and a mold temperature of 135 ℃ to 150 ℃.

Tensile strain at yield, tensile strain at break, tensile stress at yield, tensile stress at break, and tensile modulus were determined according to ISO 527 using injection molded test specimens.

Notched Izod impact strength was determined by ISO 180/A using injection molded test specimens.

The polymer compositions and the test results of the examples and comparative examples are shown in tables 1-3 below.

TABLE 1

Examples C1, C2, and E3 show unfilled compositions comprising PPS washed with acetic acid, water, and zinc acetate, respectively. As shown above, the composition of example E3 with zinc acetate washed PPS unexpectedly exhibited a significantly higher melt crystallization temperature (Tmc) of 225 ℃ compared to comparative examples C1 and C2 (189 ℃ and 199 ℃, respectively). Examples C4, C5, C6, and E7 show glass fiber filled compositions comprising PPS washed with acetic acid, water, potassium hydroxide, and zinc acetate, respectively. As shown above, the composition of example E7 with zinc acetate washed PPS unexpectedly exhibited a significantly higher Tmc of 230 ℃ compared to comparative examples C4, C5, and C6 (220 ℃, 212 ℃, and 201 ℃, respectively).

TABLE 2

Examples C8, C9, C10, and E11 show impact modifiers having a different impact strength than those used in the previous examples (C)AX8900) and comprises glass fiber-filled compositions of PPS washed with acetic acid, water, calcium acetate, and zinc acetate, respectively. As shown in table 2 above, the composition of example E11 with zinc acetate washed PPS unexpectedly exhibited a significantly higher Tmc of 229 ℃ compared to comparative examples C8, C9, and C10 (216 ℃, 221 ℃, and 214 ℃, respectively).

Similarly, examples C12, C13, C14, and E15 show impact modifiers having differences from those used in the previous examples (C: (C))AS) and including a glass fiber filled composition of PPS washed with acetic acid, water, calcium acetate, and zinc acetate, respectively. As shown in table 2, the composition of example E15 with PPS washed with zinc acetate unexpectedly exhibited a significantly higher Tmc of 229 ℃ compared to comparative examples C12, C13, and C14 (213 ℃, 217 ℃, and 209 ℃, respectively).

TABLE 3

Example E21 is a polymer composition comprising a 1:2 by weight mixture of acetic acid washed PPS and zinc acetate washed PPS. This polymer composition has a zinc content of only 1090ppm, however it unexpectedly exhibits a Tmc of 226 ℃, which is comparable to the zinc content of the same polymer composition containing only zinc acetate washed PPS (i.e., example E15, having a PPS zinc content of 1630ppm and a Tmc of 229 ℃).

The above embodiments are intended to be illustrative and not restrictive. Further embodiments are within the inventive concept. Furthermore, although the present invention has been described with reference to particular embodiments, workers skilled in the art will recognize that changes may be made in form and detail without departing from the spirit and scope of the invention. Any incorporation by reference of documents above is limited such that no subject matter is incorporated that is contrary to the explicit disclosure herein.